Polymerization catalysts for producing polymers with high comonomer incorporation

ABSTRACT

The present techniques relate to catalyst compositions, methods, and polymers encompassing a Group 4 metallocene compound comprising bridged η 5 -cyclopentadienyl-type ligands, typically in combination with a cocatalyst, and an activator. The bridged η 5 -cyclopentadienyl-type ligands are connected by a cyclic substituent.

CROSS-REFERENCE TO RELATED APPLICATIONS

This application is a continuation of U.S. patent application Ser. No.12/856,493, filed on Aug. 13, 2010, which is a divisional of U.S. patentapplication Ser. No. 11/904,728, now U.S. Pat. No. 7,799,721, filed onSep. 28, 2007, both of which are incorporated by reference herein intheir entirety.

BACKGROUND OF THE INVENTION

The present techniques relate to the field of organometalliccompositions, olefin polymerization catalyst compositions, and methodsfor the polymerization and copolymerization of olefins using a catalystcomposition.

This section is intended to introduce the reader to aspects of art thatmay be related to aspects of the present invention, which are describedand/or claimed below. Accordingly, it should be understood that thesestatements are to be read in this light, and not as admissions of priorart.

Polyolefins can be made using catalysts and various types ofpolymerization reactors that cause the combination of various monomers,such as alpha olefins, into chains of polymer. These alpha olefins areobtained from processing hydrocarbons, such as oil, into variouspetrochemicals. Different properties may be obtained if two or moredifferent alpha-olefin monomers are polymerized to form a copolymer. Ifthe same alpha-olefin is used for polymerization, the polymer can bereferred to as a homopolymer. As these polymer chains are developedduring polymerization, they can form solid particles, such as fluff orgranules, which possess certain properties and impart various mechanicaland physical properties to end products comprising these polymers.

Products made from polyolefins have become increasingly prevalent insociety as plastic products. One benefit of these polyolefins is thatthey are generally non-reactive when put in contact with various goodsor products. In particular, plastic products from polyolefin polymers(such as polyethylene, polypropylene, and their copolymers) are used forretail and pharmaceutical packaging (such as display bags, bottles, andmedication containers), food and beverage packaging (such as juice andsoda bottles), household and industrial containers (such as pails, drumsand boxes), household items (such as appliances, furniture, carpeting,and toys), automobile components, fluid, gas and electrical conductionproducts (such as cable wrap, pipes, and conduits), and various otherindustrial and consumer products.

Many methods are used for the manufacture of products from polyolefins,including but not limited to, blow-molding injection-molding, rotationalmolding, various extrusion methods, thermoforming, sheet molding andcasting. The mechanical requirements of the end-product application,such as tensile strength and density, and/or the chemical requirements,such as thermal stability, molecular weight, and chemical reactivity,typically determine what type of polyolefin is suitable and provides thebest processing capabilities during manufacture.

BRIEF DESCRIPTION OF THE FIGURES

Advantages of the invention may become apparent upon reading thefollowing detailed description and upon reference to the drawings inwhich:

FIG. 1 represents the chemical structures of exemplary metallocenes inaccordance with embodiments of the present techniques; and

FIG. 2 represents the chemical structures of reference metallocenes

DETAILED DESCRIPTION

One or more specific embodiments of the present invention will bedescribed below. In an effort to provide a concise description of theseembodiments, not all features of an actual implementation are describedin the specification. It should be appreciated that in the developmentof any such actual implementation, as in any engineering or designproject, numerous implementation-specific decisions must be made toachieve the developers' specific goals, such as compliance withsystem-related and business-related constraints, which may vary from oneimplementation to another. Moreover, it should be appreciated that sucha development effort might be complex and time consuming, but wouldnevertheless be a routine undertaking of design, fabrication, andmanufacture for those of ordinary skill having the benefit of thisdisclosure.

A catalyst for facilitating the polymerization of the monomers may beadded to the reactor. For example, the catalyst may be a particle addedvia a reactor feed stream and, once added, suspended in the fluid mediumwithin the reactor. The catalyst may include a support as part of orseparate from the catalyst particle. Further, a co-catalyst, such as anactivator may be added with the catalyst, or as part of the catalystparticle, to activate and/or increase the activity of the catalyst.Without these cocatalysts, the polymerization reaction may be very slow,or not occur. Activity is a measure of the performance of the catalyst,expressed as the mass of polymer produced per the mass of catalyst used.It should be noted that a polymerization catalyst is generally notstrictly consumed but typically remains as an inactive residual in thepolymer.

Catalysts that may be used in the polymerization of olefin monomer topolyolefin, e.g., ethylene to polyethylene, include organometalliccomplexes, which are organic compounds containing metal atoms, such astitanium, zirconium, vanadium, chromium, and so on. In thepolymerization, these catalysts temporarily attach to the monomer toform an active center that facilitates the sequential addition ofmonomer units to form the longer polymer chains. The catalysts are oftencombined with a support or activator-support (e.g., a solid oxide). Inaddition, the metal catalyst and solid oxide may be blended with acocatalyst to further activate the catalyst for polymerization. Catalystcompositions of organometallic complexes may be useful both forhomopolymerization of ethylene and for copolymerization of ethylene withcomonomers such as propylene, 1-butene, 1-hexene, or other higherα-olefins.

The incorporation of comonomers lowers the crystallinity, melting point,and density of the polymers. This results in a polymer that is both lessstiff and higher impact than a homopolymer of equivalent molecularweight. More importantly, the ability to modify the amount and type ofcomonomer allows the properties of the polymer to be tailored forspecific applications. Examples of such tailoring may include milkbottles, which may require a stiff, high density polyethylene, tostretch film resins, which may require a very low density, flexiblepolyethylene.

Effective copolymerization may often require that the comonomer be addedto the reactor in significantly higher concentrations than present inthe final polymer. This is a result of lower than desirableincorporation of the comonomer into the polymer chain. This lowincorporation lowers the efficiency of the process, increasing the costsfor production. Further, certain types of catalysts may show poorcomonomer incorporation, limiting their use in the formation ofcopolymers.

Many types of catalyst systems for producing polyolefins do notefficiently incorporate co-monomers. Accordingly, these catalystssystems may not be ideal for the production of low density resins. Incontrast to other catalyst systems, however, certain metallocenecatalysts can be effective at incorporating comonomers, and may beuseful in the production of low density resins. Further, metallocenecatalysts made in accordance with the present techniques may incorporatecomonomer at higher rates than current metallocene catalysts used toproduce low-density resins (<0.92 g/cc) in slurry processes.Accordingly, the metallocenes of the present techniques may be usefulfor the production of elastomers in a slurry process.

The present techniques include new catalyst compositions, methods forpreparing catalyst compositions, and methods for using the catalystcompositions to polymerize olefins. In some embodiments, the techniquesencompass a catalyst composition prepared by contacting atightly-bridged ansa-metallocene compound including a cyclic bridginggroup connecting two η⁵-cyclopentadienyl type ligands, an activator, andoptionally an organoaluminum compound. The catalyst composition formedas the contact product may include the contacted compounds, reactionproducts formed from the contacted compounds, or both. Such a catalystcomposition may have improved comonomer incorporation over other typesof metallocene systems. In other embodiments, the present techniquesinclude methods for making the catalyst composition presented herein,and in still other embodiments, the present techniques include methodsfor polymerizing olefins employing the catalyst composition presentedherein. As described above, the designation of the organoaluminumcompound as an optional component in the contact product is intended toreflect that the organoaluminum compound may be optional when it may notbe necessary to impart catalytic activity to the composition includingthe contact product, as understood by one of ordinary skill in the art.To facilitate discussion of the current techniques, the disclosurescontained herein are presented in sections.

Section I presents catalyst compositions and components in accordancewith embodiments of the present techniques. The catalyst compositionsand components include exemplary metallocene compounds, optionalorganoaluminum compounds, activators/cocatalysts, nonlimiting examplesof catalyst compositions, and olefin monomers that may be employed inthe present techniques.

Section II presents techniques for the preparation of exemplary catalystcompositions using the components discussed in Section I. Thesepreparations include the precontacting of the catalyst compositions witholefins, the use of multiple precontacting steps, the composition ratiosthat may be used in catalyst compositions of the present techniques,exemplary catalyst preparation processes, and the activities ofcatalysts (in terms of polymer produced per weight catalyst per hour)that may be obtained from the catalyst compositions of the presenttechniques.

Section III discusses various processes that the catalyst compositionsof the present techniques may be used in for polymerization. Particularprocesses discussed included loop slurry polymerizations, gas phasepolymerizations, and solution phase polymerizations. Other informationrelevant to the implementation of the catalyst compositions of thecurrent techniques are also presented in this section, including plantsystems for feed to and polymer removal from the reactors, particularpolymerization conditions, and exemplary products that may be made frompolymers formed using the catalyst compositions of the presenttechniques.

Section IV presents non-limiting examples of polymers prepared usingcatalyst compositions in accordance with embodiments of the presenttechniques. The examples include data indicating the improvements incomonomer incorporation that may be obtained for polymers made usingexemplary catalyst compositions of the present techniques. The resultsthat may be obtained for molecular weights and catalyst activities usingthe exemplary catalyst compositions are also discussed.

Section V presents experimental procedures that may be used to make andtest exemplary catalyst compositions in accordance with embodiments ofthe present techniques. A method for the determination of pore size isdiscussed. Further, the section includes a discussion of a techniquethat may be used for the measurement of comonomer incorporation. SectionV also discusses exemplary techniques for synthesis of the variouspolymer components. These procedures include techniques for making thefluorided silica-alumina and sulfated alumina activator-supports. Theprocedures also include techniques for making exemplary metallocenes andpolymers, in accordance with embodiments of the present techniques.

I. Catalyst Composition and Components

A. The Metallocene Compounds

1. Overview

In one embodiment, the present techniques may include a catalystcomposition having a tightly-bridged ansa-metallocene compound includingan alkyl or alkenyl group bonded to a cyclopentadienyl ligand, anactivator, and, optionally, an organoaluminum compound. A generaldescription of the ansa-metallocene complex is presented in thefollowing subsection 2.

The term “bridged” or “ansa-metallocene” may refer to a metallocenecompound in which the two η⁵-cycloalkadienyl-type ligands in themolecule are linked by a bridging moiety. Useful ansa-metallocenes maybe “tightly-bridged,” meaning that the two η⁵-cycloalkadienyl-typeligands are connected by a bridging group wherein the shortest link ofthe bridging moiety between the η⁵-cycloalkadienyl-type ligands is asingle atom. The metallocenes described herein are therefore bridgedbis(η⁵-cycloalkadienyl)-type compounds. The bridging group connectingthe η⁵-cycloalkadienyl-type ligands may have the formula E(Cyc), whereinE may be a carbon atom, a silicon atom, a germanium atom, or a tin atom,and E is bonded to both X¹ and X², and wherein Cyc may be a substitutedor an unsubstituted carbon chain of from 4 to 6 carbon atoms in lengthwith each end connected to E to form a ring structure (herein referredto as “a cyclic bridging moiety”).

In various embodiments, the bridging group, E(Cyc), may have the generalformula: >C(Cyc), >Si(Cyc), >Ge(Cyc), or >Sn(Cyc), wherein Cyc may be asubstituted or an unsubstituted carbon chain of from 4 to 6 carbon atomsin length with each end connected to E to form a ring structure. Suchbridging E(Cyc) groups may include, for example, >C(CH₂CH₂CH₂CH₂),>C(CH₂CH₂CH₂CH₂CH₂), >Si(CH₂CH₂CH₂CH₂), >Si(CH₂CH₂CH₂CH₂CH₂),>Ge(CH₂CH₂CH₂CH₂), >Ge(CH₂CH₂CH₂CH₂CH₂), >Sn(CH₂CH₂CH₂CH₂), and>Sn(CH₂CH₂CH₂CH₂CH₂), among others. In these examples, each end of thecarbon chain is connected to the initial carbon. The Cyc group may alsobe substituted at one of more points by any of the groups listed below.

Further, one substituent on the η⁵-cyclopentadienyl-type ligands may bea substituted or an unsubstituted alkyl, or alkenyl group, having up to12 carbon atoms. In embodiments of the present techniques, the alkyl oralkenyl group may be bonded to the η⁵-cyclopentadienyl ligand. Theseembodiments are seen in the general structural formulas presented in thefollowing subsection 3. Exemplary metallocene complexes, in accordancewith embodiments of the present invention are shown in the followingsubsection 4.

2. General Metallocene Formula

In embodiments of the present techniques, the ansa-metallocene of thepresent techniques may be expressed by the general formula:(X¹)(X²)(X³)(X⁴)M¹.In this formula, M¹ may be titanium, zirconium, or hafnium, X¹ and X²are independently a substituted cyclopentadienyl, a substituted indenyl,or a substituted fluorenyl. One substituent on X¹ and X² is a bridginggroup having the formula E(Cyc), wherein E may be a carbon atom, asilicon atom, a germanium atom, or a tin atom, and E is bonded to bothX¹ and X², and wherein Cyc may be a substituted or an unsubstitutedcarbon chain of from 4 to 6 carbon atoms in length with each endconnected to E to form a ring structure. In embodiments of the presenttechniques, one substituent on the η⁵-cyclopentadienyl-type ligands maybe a substituted or an unsubstituted alkyl or alkenyl group having up to12 carbon atoms. Substituents X³ and X⁴ may be independently: F, Cl, Br,or I; a hydrocarbyl group having up to 20 carbon atoms, H, or BH₄; ahydrocarbyloxide group, a hydrocarbylamino group, or atrihydrocarbylsilyl group, any of which may have up to 20 carbon atoms;and/or OBR^(A) ₂ or SO₃R^(A), wherein R^(A) may be an alkyl group or anaryl group, either of which may have up to 12 carbon atoms. Anyadditional substituent on the substituted cyclopentadienyl, substitutedindenyl, substituted fluorenyl, substituted alkyl or alkenyl group, oron Cyc may be independently an aliphatic group, an aromatic group, acyclic group, a combination of aliphatic and cyclic groups, an oxygengroup, a sulfur group, a nitrogen group, a phosphorus group, an arsenicgroup, a carbon group, a silicon group, or a boron group, any of whichmay have from 1 to 20 carbon atoms. Alternatively, additionalsubstituents may be present, including halides or hydrogen.

The alkyl or alkenyl group bonded to the η⁵-cyclopentadienyl-typeligands may have up to about 20 carbon atoms. In an exemplaryembodiment, the alkyl or alkenyl group may have up to about 12 carbonatoms, up to about 8 carbon atoms, or up to about 6 carbon atoms.Exemplary alkyl groups may include butyl, pentyl, hexyl, heptyl, oroctyl, among others. Exemplary alkenyl groups may include 3-butenyl,4-pentenyl, 5-hexenyl, 6-heptenyl, or 7-octenyl, among others.

While the alkyl or alkenyl substituent on the η⁵-cyclopentadienyl-typeligands may be unsubstituted, alternatively, the alkyl or alkenyl groupmay be substituted. Any substituent present may be selectedindependently from an aliphatic group, an aromatic group, a cyclicgroup, a combination of aliphatic and cyclic groups, an oxygen group, asulfur group, a nitrogen group, a phosphorus group, an arsenic group, acarbon group, a silicon group, a boron group, or a substituted analogthereof, any of which may have from 1 to about 20 carbon atoms. Thesubstituents may also include a halide or hydrogen. Further, thisdescription of other substituents on the alkyl or alkenyl group mayinclude substituted, unsubstituted, branched, linear, orheteroatom-substituted analogs of these moieties.

In addition to containing a bridging group having the formula E(Cyc) andan alkyl or alkenyl group as described above, theη⁵-cyclopentadienyl-type ligands may also have other substituents. Forexample, these substituents may be the same chemical groups or moietiesthat can serve as the X³ and X⁴ ligands of the ansa-metallocenes. Thus,any additional substituent on the η⁵-cyclopentadienyl-type ligands, anysubstituent on the substituted alkyl or alkenyl group, any substituenton the Cyc group, X³ and X⁴ may be independently groups including analiphatic group, an aromatic group, a cyclic group, a combination ofaliphatic and cyclic groups, an oxygen group, a sulfur group, a nitrogengroup, a phosphorus group, an arsenic group, a carbon group, a silicongroup, a boron group, or a substituted analog thereof, any of whichhaving from 1 to about 20 carbon atoms. The substituents may alsoinclude a halide or hydrogen, as long as these groups do not terminatethe activity of the catalyst composition. Further, this list may includesubstituents that may be characterized in more than one of thesecategories, such as benzyl. Substituents may also include substitutedindenyl and substituted fluorenyl, including partially saturatedindenyls and fluorenyls such as, for example, tetrahydroindenyl groups,tetrahydrofluorenyl groups, and octahydrofluorenyl groups. Examples ofeach of these substituent groups are discussed below.

Aliphatic groups that may be used as substituents include, for example,an alkyl group, a cycloalkyl group, an alkenyl group, a cycloalkenylgroup, an alkynyl group, an alkadienyl group, a cyclic group, and thelike. This may include all substituted, unsubstituted, branched, andlinear analogs or derivatives thereof, wherein each group may have fromone to about 20 carbon atoms. Thus, aliphatic groups may include, forexample, hydrocarbyls such as paraffins and alkenyls. For example, thealiphatic groups may include such groups as methyl, ethyl, propyl,n-butyl, tert-butyl, sec-butyl, isobutyl, amyl, isoamyl, hexyl,cyclohexyl, heptyl, octyl, nonyl, decyl, dodecyl, 2-ethylhexyl,pentenyl, butenyl, and the like.

Aromatic groups that may be used as substituents include, for example,phenyl, naphthyl, anthracenyl, and the like. Substituted derivatives ofthese compounds are also included, wherein each group may have from 6 toabout 25 carbons. Such substituted derivatives may include, for example,tolyl, xylyl, mesityl, and the like, including any heteroatomsubstituted derivatives thereof.

Cyclic groups that may be used as substituents include, for example,cycloparaffins, cycloolefins, cycloacetylenes, arenes such as phenyl,bicyclic groups and the like, as well as substituted derivativesthereof, in each occurrence having from about 3 to about 20 carbonatoms. Thus, substituted heteroatom-substituted cyclic groups such asfuranyl may be included herein. Such substituents may include, aliphaticand cyclic groups, e.g., groups that have both an aliphatic portion anda cyclic portion. Examples of these substituents may include groups suchas: —(CH₂)_(m)C₆H_(q)R_(5-q) wherein m may be an integer from 1 to about10, and q may be an integer from 1 to 5, inclusive;—(CH₂)_(m)C₆H_(q)R_(11-q) wherein m may be an integer from 1 to about10, and q may be an integer from 1 to 11, inclusive; or—(CH₂)_(m)C₅H_(q)R_(9-q) wherein m may be an integer from 1 to about 10,and q may be an integer from 1 to 9, inclusive. As defined above, R maybe independently selected from: an aliphatic group; an aromatic group; acyclic group; any combination thereof; any substituted derivativethereof, including, but not limited to, a halide-, an alkoxide-, or anamide-substituted derivative or analog thereof; any of which has from 1to about 20 carbon atoms; or hydrogen. In various embodiments, suchaliphatic and cyclic groups may include, for example: —CH₂C₆H₅;—CH₂C₆H₄F; —CH₂C₆H₄Cl; —CH₂C₆H₄Br; —CH₂C₆H₄I; —CH₂C₆H₄OMe; —CH₂C₆H₄OEt;—CH₂C₆H₄NH₂; —CH₂C₆H₄NMe₂; —CH₂C₆H₄NEt₂; —CH₂CH₂C₆H₅; —CH₂CH₂C₆H₄F;—CH₂CH₂C₆H₄Cl; —CH₂CH₂C₆H₄Br; —CH₂CH₂C₆H₄₁; —CH₂CH₂C₆H₄OMe;—CH₂CH₂C₆H₄OEt; —CH₂CH₂C₆H₄NH₂; —CH₂CH₂C₆H₄NMe₂; —CH₂CH₂C₆H₄NEt₂; anyregioisomer thereof, and any substituted derivative thereof.

Substituents may contain heteroatoms, including halides, oxygen, sulfur,nitrogen, phosphorous, or arsenic. Examples of halides include fluoride,chloride, bromide, and iodide. As used herein, oxygen groups areoxygen-containing groups, including, for example, alkoxy or aryloxygroups (—OR) and the like, wherein R may be alkyl, cycloalkyl, aryl,aralkyl, substituted alkyl, substituted aryl, or substituted aralkylhaving from 1 to about 20 carbon atoms. Such alkoxy or aryloxy groups(—OR) groups may include, for example, methoxy, ethoxy, propoxy, butoxy,phenoxy, or substituted phenoxy, among others. As used herein, sulfurgroups are sulfur-containing groups, including, for example, —SR and thelike, wherein R in various embodiments may be alkyl, cycloalkyl, aryl,aralkyl, substituted alkyl, substituted aryl, or substituted aralkylhaving from 1 to about 20 carbon atoms. As used herein, nitrogen groupsare nitrogen-containing groups, which may include, for example, —NR₂ orpyridyl groups, and the like, wherein R in various embodiments may bealkyl, cycloalkyl, aryl, aralkyl, substituted alkyl, substituted aryl,or substituted aralkyl having from 1 to about 20 carbon atoms. As usedherein, phosphorus groups are phosphorus-containing groups, which mayinclude, for example, —PR₂, and the like, wherein R in variousembodiments may be alkyl, cycloalkyl, aryl, aralkyl, substituted alkyl,substituted aryl, or substituted aralkyl having from 1 to about 20carbon atoms. As used herein, arsenic groups are arsenic-containinggroups, which may include, for example, —AsR₂, and the like, wherein Rin various embodiments may be alkyl, cycloalkyl, aryl, aralkyl,substituted alkyl, substituted aryl, or substituted aralkyl having from1 to about 20 carbon atoms.

As used herein, carbon groups are carbon-containing groups, which mayinclude, for example, alkyl halide groups. Such alkyhalide groups mayinclude halide-substituted alkyl groups with 1 to about 20 carbon atoms,alkenyl or alkenyl halide groups with 1 to about 20 carbon atoms,aralkyl or aralkyl halide groups with 1 to about 20 carbon atoms, andthe like, including substituted derivatives thereof.

As used herein, silicon groups are silicon-containing groups, which mayinclude, for example, silyl groups such alkylsilyl groups, arylsilylgroups, arylalkylsilyl groups, siloxy groups, and the like, having from1 to about 20 carbon atoms. For example, silicon groups includetrimethylsilyl and phenyloctylsilyl groups.

As used herein, boron groups are boron-containing groups, which mayinclude, for example, —BR₂, —BX₂, —BRX, wherein X may be a monoanionicgroup such as halide, hydride, alkoxide, alkyl thiolate, and the R invarious embodiments may be alkyl, cycloalkyl, aryl, aralkyl, substitutedalkyl, substituted aryl, or substituted aralkyl having from 1 to about20 carbon atoms.

The remaining substituents on the metal center, X³ and X⁴′ may beindependently an aliphatic group, a cyclic group, a combination of analiphatic group and a cyclic group, an amido group, a phosphido group,an alkyloxide group, an aryloxide group, an alkanesulfonate, anarenesulfonate, or a trialkylsilyl, or a substituted derivative thereof,any of which having from 1 to about 20 carbon atoms; or a halide. Morespecifically, X³ and X⁴ may be independently: F, Cl, Br, or I; ahydrocarbyl group having up to 20 carbon atoms, H, or BH₄; ahydrocarbyloxide group, a hydrocarbylamino group, or atrihydrocarbylsilyl group, any of which having up to 20 carbon atoms;OBR^(A) ₂ or SO₃R^(A), wherein R^(A) may be an alkyl group or an arylgroup, any of which having up to 12 carbon atoms.

3. General Structural Formulas for Metallocene Catalysts

Embodiments of the current techniques may include an ansa-metallocenehaving the formula:

wherein M¹ may be zirconium or hafnium and X′ and X″ may beindependently F, Cl, Br, or I. E may be C or Si and n may be an integerfrom 1 to 3 inclusive. R^(3A) and R^(3B) may be independently ahydrocarbyl group or a trihydrocarbylsilyl group, any of which may haveup to 20 carbon atoms, or may be hydrogen. The subscript ‘m’ may be aninteger that may range from 0 to 10, inclusive. R^(4A) and R^(4B) may beindependently a hydrocarbyl group that may have up to 12 carbon atoms,or may be hydrogen. Bond ‘a’ may be a single or a double bond.

In other embodiments, the ansa-metallocene may include a compound havingthe formula:

In this formula, M¹ may be zirconium or hafnium, and X′ and X″ may beindependently F, Cl, Br, or I. E may be C or Si and ‘n’ may be aninteger from 1 to 3, inclusive. R^(3A) and R^(3B) may be independentlyH, methyl, ethyl, propyl, allyl, benzyl, butyl, pentyl, hexyl, ortrimethylsilyl, and ‘m’ may be an integer from 1 to 6, inclusive. R^(4A)and R^(4B) may be independently a hydrocarbyl group having up to 6carbon atoms, or hydrogen. Bond ‘a’ may be a single or a double bond.

In still other embodiments, the ansa-metallocene may include a compoundhaving the formula:

In this formula, M¹ may be zirconium or hafnium, and X′ and X″ may beindependently F, Cl, Br, or I. E may be C or Si and ‘n’ may be 1 or 2.R^(3A) and R^(3B) may be independently H or methyl, and ‘m’ may be 1 or2. R^(4A) and R^(4B) may be independently H or t-butyl. Bond ‘a’ may bea single or a double bond.

In yet other embodiments, the ansa-metallocene of the present techniquesmay include a compound having the formula:

In this formula, M¹ may be zirconium or hafnium, and X′ and X″ may beindependently H, BH₄, methyl, phenyl, benzyl, neopentyl,trimethylsilylmethyl, CH₂CMe₂Ph; CH₂SiMe₂Ph; CH₂CMe₂CH₂Ph; orCH₂SiMe₂CH₂Ph. E may be C or Si and n may be an integer from 1 to 3,inclusive. R^(3A) and R^(3B) may be independently a hydrocarbyl group ora trihydrocarbylsilyl group, any of which having up to 20 carbon atoms,or hydrogen, and n may be an integer from 0 to 10, inclusive. R^(4A) andR^(4B) may be independently a hydrocarbyl group having up to 12 carbonatoms, or hydrogen. Bond ‘a’ may be a single or a double bond.

4. Non-Limiting Examples of Metallocene Structures

In exemplary embodiments, the ansa-metallocene may include either ofcompounds (I-1) or (I-2), as shown in FIG. 1, or any combinationthereof. Numerous processes to prepare metallocene compounds that may beemployed in the present techniques have been reported. For example, U.S.Pat. Nos. 4,939,217, 5,191,132, 5,210,352, 5,347,026, 5,399,636,5,401,817, 5,420,320, 5,436,305, 5,451,649, 5,496,781, 5,498,581,5,541,272, 5,554,795, 5,563,284, 5,565,592, 5,571,880, 5,594,078,5,631,203, 5,631,335, 5,654,454, 5,668,230, 5,705,578, 5,705,579,6,187,880, and 6,509,427 describe such methods, each of which isincorporated by reference in its entirety herein.

B. The Optional Organoaluminum Compounds

In one embodiment, the present techniques may include a catalystcomposition including a tightly-bridged ansa-metallocene compound havinga cyclic bridging moiety attached to both η⁵-cyclopentadienyl-typeligands, a solid oxide activator-support, and, optionally, anorganoaluminum compound. The designation of the organoaluminum compoundas “optional” is intended to reflect that the organoaluminum compoundmay be optional when it may not be necessary to impart catalyticactivity to the composition including the contact product, as understoodby one of ordinary skill, as presented herein.

Organoaluminum compounds that may be used in the present techniquesinclude, for example, compounds with the formula:Al(X⁵)_(n)(X⁶)_(3-n),wherein X⁵ may be a hydrocarbyl having from 1 to about 20 carbon atoms;X⁶ may be alkoxide or aryloxide, any of which having from 1 to about 20carbon atoms, halide, or hydride; and n may be a number from 1 to 3,inclusive. X⁵ may be an alkyl having from 1 to about 10 carbon atoms.Moieties used for X⁵ may include, for example, methyl, ethyl, propyl,butyl, sec-butyl, isobutyl, 1-hexyl, 2-hexyl, 3-hexyl, isohexyl, heptyl,or octyl, and the like. Alternatively, X⁶ may be independently fluoride,chloride, bromide, methoxide, ethoxide, or hydride. In yet anotherembodiment, X⁶ may be chloride.

In the formula Al(X⁵)_(n)(X⁶)_(3-n), n may be a number from 1 to 3inclusive, and in an exemplary embodiment, n may be 3. The value of n isnot restricted to an integer, therefore this formula may includesesquihalide compounds, other organoaluminum cluster compounds, and thelike.

Generally, organoaluminum compounds that may be used in the presenttechniques may include trialkylaluminum compounds, dialkylaluminiumhalide compounds, dialkylaluminum alkoxide compounds, dialkylaluminumhydride compounds, and combinations thereof. Examples of suchorganoaluminum compounds include trimethylaluminum, triethylaluminum(TEA), tripropylaluminum, tributylaluminum, tri-n-butylaluminum (TNBA),triisobutylaluminum (TIBA), trihexylaluminum, triisohexylaluminum,trioctylaluminum, diethylaluminum ethoxide, diisobutylaluminum hydride,or diethylaluminum chloride, or any combination thereof. If theparticular alkyl isomer is not specified, the compound may encompass allisomers that can arise from a particular specified alkyl group.

In some embodiments, the present techniques may include precontactingthe ansa-metallocene with an organoaluminum compound and an olefinmonomer to form a precontacted mixture, prior to contacting thisprecontacted mixture with the solid oxide activator-support to form theactive catalyst. When the catalyst composition is prepared in thismanner, a portion of the organoaluminum compound may be added to theprecontacted mixture and another portion of the organoaluminum compoundmay be added to the postcontacted mixture prepared when the precontactedmixture is contacted with the solid oxide activator. However, all of theorganoaluminum compound may be employed to prepare the catalyst ineither the precontacting or postcontacting step. Alternatively, thesolid oxide may also be treated with aluminum alkyl before being treatedwith metallocene or other mixtures. These precontacting steps are notrequired, and all of the catalyst components may be contacted in asingle step.

Further, more than one organoaluminum compound may be used, in eitherthe precontacting or the postcontacting step, or in any procedure inwhich the catalyst components are contacted. When an organoaluminumcompound is added in multiple steps, the amounts of organoaluminumcompound presented herein include the total amount of organoaluminumcompound used in both the precontacted and postcontacted mixtures, andany additional organoaluminum compound added to the polymerizationreactor. Therefore, total amounts of organoaluminum compounds arepresented, regardless of whether a single organoaluminum compound isused, or more than one organoaluminum compound. Again, exemplaryorganoaluminum compounds used in embodiments of the present techniquesmay include, for example, triethylaluminum (TEA), tri-n-butylaluminum,triisobutylaluminum, and so on, or any combination thereof.

C. The Activator/Cocatalyst

1. Overview

Embodiments of the present techniques encompass a catalyst compositionincluding a tightly-bridged ansa-metallocene compound as presentedherein; optionally, an organoaluminum compound; and an activator. Theactivator may be used to weaken the bonds between the metal center andligands X³ or X⁴, allowing complexation of the metal center with anolefin. Further, an activator or co-catalyst may replace X³ or X⁴ with acarbon group having a single-bond to the metal. The activator may be anactivator-support including a solid oxide treated with anelectron-withdrawing anion, as discussed in the following subsection 2;an ion-exchangeable or layered mineral activator-support, as discussedin the following subsection 3; an organoaluminoxane compound, asdiscussed in the following subsection 4; an organoboron or organoboratecompound, as discussed in the following subsection 5; or an ionizingcompound, as discussed in the following subsection 6; or any combinationof any of these activators.

In some embodiments of the present techniques, aluminoxane may not berequired to form the catalyst composition as presented herein.Accordingly, in some embodiments, AlR₃-type organoaluminum compounds andone or more activator-supports may be used in the absence ofaluminoxanes. While not intending to be bound by theory, it is believedthat the organoaluminum compounds may not activate the metallocenecatalysts in the same manner as an organoaluminoxane.

Additionally, no borate compounds or MgCl₂ may be required to form thecatalyst composition of the present techniques, although aluminoxane,borate compounds, MgCl₂, or any combination thereof, may optionally beused in the catalyst composition of the present techniques. Further, insuch compounds as aluminoxanes, organoboron compounds, ionizing ioniccompounds, or any combination thereof, may be used as cocatalysts withthe ansa-metallocene, either in the presence or absence of the activatorsupport. Such cocatalysts may be used with the ansa-metallocene, eitherin the presence or absence of an organoaluminum compound, as specifiedherein. Thus, the organoaluminum compound may be optional: when a ligandon the metallocene is a hydrocarbyl group, H, or BH₄; when the activatorincludes an organoaluminoxane compound; or when both these conditionsare present. However, the catalyst compositions of the presenttechniques may be active in the substantial absence of cocatalysts suchas aluminoxanes, organoboron compounds, ionizing ionic compounds, or anycombination thereof.

2. Chemically-Treated Solid Oxide Activator-Supports

a. Overview

The present techniques encompass catalyst compositions that include anacidic activator-support, such as, for example, a chemically-treatedsolid oxide (CTSO). A CTSO may be used in combination with anorganoaluminum compound. The activator-support may include a solid oxidetreated with an electron-withdrawing anion. The solid oxide may includesuch compounds as silica, alumina, silica-alumina, aluminophosphate,aluminum phosphate, zinc aluminate, heteropolytungstates, titania,zirconia, magnesia, boria, zinc oxide, mixed oxides thereof, and thelike, or any mixture or combination thereof. The electron-withdrawinganion may include fluoride, chloride, bromide, iodide, phosphate,triflate, bisulfate, sulfate, fluoroborate, fluorosulfate,trifluoroacetate, phosphate, fluorophosphate, fluorozirconate,fluorosilicate, fluorotitanate, permanganate, substituted orunsubstituted alkanesulfonate, substituted or unsubstitutedarenesulfonate, substituted or unsubstituted alkylsulfate, or anycombination thereof.

The activator-support may include the contact product of a solid oxidecompound and an electron-withdrawing anion source, as presented in thefollowing subsection b. The solid oxide compound may include aninorganic oxide, and may be optionally calcined prior to contacting theelectron-withdrawing anion source. The contact product may also becalcined either during or after the solid oxide compound is contactedwith the electron-withdrawing anion source. In this embodiment, thesolid oxide compound may be calcined or uncalcined. In anotherembodiment, the activator-support may include the contact product of acalcined solid oxide compound and an electron-withdrawing anion source.

The treated activator-support may exhibit enhanced activity as comparedto the corresponding untreated solid oxide compound. While not intendingto be bound by theory, it is believed that the activator-support canfunction as a solid oxide supporting compound with an additionalionizing, polarizing, or bond weakening function, collectively termed an“activating” function, by weakening the metal-ligand bond between ananionic ligand and the metal in the metallocene. Thus, theactivator-support may be considered to exhibit an “activating” function,regardless of whether it ionizes the metallocene, abstracts an anionicligand to form an ion pair, weakens the metal-ligand bond in themetallocene, simply coordinates to an anionic ligand when it contactsthe activator-support, or any other mechanisms by which ionizing,polarizing, or bond weakening might occur. In preparing themetallocene-based catalyst compositions of the present techniques, theactivator-support is typically used along with a component that providesan activatable ligand such as an alkyl or hydride ligand to themetallocene, including but not limited to an organoaluminum compound,when the metallocene compound does not already include such a ligand. Inone embodiment the treated solid oxide may be contacted with thealuminum alkyl before being exposed to the metallocene.

The activator-support may include a solid inorganic oxide material, amixed oxide material, or a combination of inorganic oxide materials thatmay be chemically-treated with an electron-withdrawing component, andoptionally treated with another metal ion. Thus, the solid oxide of thepresent techniques encompasses oxide materials such as alumina, “mixedoxide” compounds such as silica-alumina or silica-zirconia orsilica-titania, and combinations and mixtures thereof. The mixed metaloxide compounds such as silica-alumina, with more than one metalcombined with oxygen to form a solid oxide compound, may be made byco-gellation, impregnation or chemical deposition, and are encompassedby the present techniques.

Further, the activator-support may include an additional metal or metalion such as zinc, nickel, vanadium, silver, copper, gallium, tin,tungsten, molybdenum, or any combination thereof. Examples ofactivator-supports that further include a metal or metal ion include,for example, zinc-impregnated chlorided alumina, zinc-impregnatedfluorided alumina, zinc-impregnated chlorided silica-alumina,zinc-impregnated fluorided silica-alumina, zinc-impregnated sulfatedalumina, or any combination thereof.

The activator-support of the present techniques may include a solidoxide of relatively high porosity, which exhibits Lewis acidic orBrønsted acidic behavior. The solid oxide may be chemically-treated withan electron-withdrawing component, typically an electron-withdrawinganion, to form an activator-support. While not intending to be bound bytheory, it is believed that treatment of the inorganic oxide with anelectron-withdrawing component augments or enhances the acidity of theoxide. Thus, the activator-support exhibits Lewis or Brønsted aciditywhich may be typically greater than the Lewis or Brønsted acidity of theuntreated solid oxide. The polymerization activity of thechemically-treated solide oxide may be enhanced over the activity shownby an untreated solid oxide.

The chemically-treated solid oxide may include a solid inorganic oxide,including oxygen and an element selected from Group 2, 3, 4, 5, 6, 7, 8,9, 10, 11, 12, 13, 14, or 15 of the periodic table, or including oxygenand an element selected from the lanthanide or actinide elements. Forexample, the inorganic oxide may include oxygen and an element selectedfrom Al, B, Be, Bi, Cd, Co, Cr, Cu, Fe, Ga, La, Mn, Mo, Ni, Sb, Si, Sn,Sr, Th, Ti, V, W, P, Y, Zn or Zr.

Suitable solid oxide materials or compounds that may be used in thechemically-treated solid oxide of the present techniques may include,for example, Al₂O₃, B₂O₃, BeO, Bi₂O₃, CdO, CO₃O₄, Cr₂O₃, CuO, Fe₂O₃,Ga₂O₃, La₂O₃, Mn₂O₃, MoO₃, NiO, P₂O₅, Sb₂O₅, SiO₂, SnO₂, SrO, ThO₂,TiO₂, V₂O₅, WO₃, Y₂O₃, ZnO, ZrO₂, and the like, including mixed oxidesthereof, and combinations thereof. Mixed oxides that may be used in theactivator-support of the present techniques may include, for example,mixed oxides of any combination of Al, B, Be, Bi, Cd, Co, Cr, Cu, Fe,Ga, La, Mn, Mo, Ni, P, Sb, Si, Sn, Sr, Th, Ti, V, W, Y, Zn, Zr, and thelike. Examples of mixed oxides that may be used in the activator-supportof the present techniques may also include silica-alumina,silica-titania, silica-zirconia, zeolites, many clay minerals, pillaredclays, alumina-titania, alumina-zirconia, aluminophosphate, and thelike. Procedures to form such solid oxides, and exemplary chemicallytreated solid oxides are presented in the following subsections c and d,respectively. Concentrations of electron-withdrawing anions that may beuseful in forming chemically treated solid oxides are presented in thefollowing subsection e.

b. Chemical Treatment of the Solid Oxide

A solid oxide material that may be used in the present techniques may bechemically-treated by contacting it with an electron-withdrawingcomponent, typically an electron-withdrawing anion source, to cause orenhance activation of the metallocene complex. Further, the solid oxidematerial may be chemically-treated with another metal ion, that may bethe same as or different from any metal element that constitutes thesolid oxide material, then calcined to form a metal-containing ormetal-impregnated chemically-treated solid oxide. Alternatively, a solidoxide material and an electron-withdrawing anion source may be contactedand calcined simultaneously. The method by which the oxide may becontacted with an electron-withdrawing component, typically a salt or anacid of an electron-withdrawing anion, may include, for example,gelling, co-gelling, impregnation of one compound onto another,vaporization of one compound onto the other, and the like. Inembodiments of the present techniques, following any contacting method,the contacted mixture of oxide compound, electron-withdrawing anion, andoptionally the metal ion, may be calcined.

The electron-withdrawing component used to treat the oxide may be anycomponent that increases the Lewis or Brønsted acidity of the solidoxide upon treatment. In one embodiment, the electron-withdrawingcomponent is typically an electron-withdrawing anion derived from asalt, an acid, or other compound such as a volatile organic compoundthat can serve as a source or precursor for that anion. Examples ofelectron-withdrawing anions include, for example, fluoride, chloride,bromide, iodide, phosphate, trifluoromethane sulfonate (triflate),bisulfate, sulfate, fluoroborate, fluorosulfate, trifluoroacetate,phosphate, fluorophosphate, fluorozirconate, fluorosilicate,fluorotitanate, permanganate, substituted or unsubstitutedalkanesulfonate, substituted or unsubstituted arenesulfonate,substituted or unsubstituted alkylsulfate, and the like, including anymixtures and combinations thereof. In addition, other ionic or non-ioniccompounds that serve as sources for these electron-withdrawing anionsmay also be used in the present techniques. The chemically-treated solidoxide may include a sulfated solid oxide or a sulfated alumina.

The terms alkanesulfonate and alkyl sulfate refer to anions having thegeneral formula [R^(B)SO₂O]⁻ and [(R^(B)O)SO₂O]⁻, respectively, whereinR^(B) may be a linear or branched alkyl group having up to 20 carbonatoms, that may be substituted with a group selected independently fromF, Cl, Br, I, OH, OMe, OEt, OCF₃, Ph, xylyl, mesityl, or OPh. Thus, thealkanesulfonate and alkyl sulfate may be referred to as being eithersubstituted or unsubstituted. The alkyl group of the alkanesulfonate oralkyl sulfate may have up to 12 carbon atoms, up to 8 carbon atoms, orup to 6 carbon atoms. Such alkanesulfonates may include, for example,methanesulfonate, ethanesulfonate, 1-propanesulfonate,2-propane-sulfonate, 3-methylbutanesulfonate, trifluoromethanesulfonate,trichloro-methane-sulfonate, chloromethanesulfonate,1-hydroxyethanesulfonate, 2-hydroxy-2-propanesulfonate,1-methoxy-2-propanesulfonate, and the like. In other embodiments,examples of alkyl sulfates include, for example, methylsulfate,ethylsulfate, 1-propylsulfate, 2-propylsulfate, 3-methylbutylsulfate,trifluoromethanesulfate, trichloromethylsulfate, chloromethylsulfate,1-hydroxyethylsulfate, 2-hydroxy-2-propylsulfate,1-methoxy-2-propylsulfate, and the like.

The term arenesulfonate refers to anions having the general formula[Ar^(A)SO₂O]⁻, wherein Ar^(A) may be an aryl group having up to 14carbon atoms, and which may be optionally substituted with a groupselected independently from F, Cl, Br, I, Me, Et, Pr, Bu, OH, OMe, OEt,OPr, OBu, OCF₃, Ph, OPh, or Rc, wherein Rc may be a linear or branchedalkyl group having up to 20 carbon atoms. Thus, the arenesulfonate maybe referred to as a substituted or an unsubstituted arenesulfonate.Because the aryl group Ar^(A) may be substituted with an alkyl sidechain, R^(C), which may include a long alkyl side chain, the termarenesulfonate encompasses detergents. The aryl group of thearenesulfonate may have up to 10 carbon atoms, or up to 6 carbon atoms.Examples of such arenesulfonates include, for example, benzenesulfonate,naphthalenesulfonate, p-toluenesulfonate, m-toluenesulfonate,3,5-xylenesulfonate, trifluoromethoxybenzenesulfonate,trichloro-methoxybenzenesulfonate, trifluoromethyl-benzenesulfonate,trichloromethyl-benzene-sulfonate, fluorobenzenesulfonate,chlorobenzene-sulfonate, 1-hydroxy-ethane-benzenesulfonate,3-fluoro-4-methoxybenzenesulfonate, and the like.

When the electron-withdrawing component includes a salt of anelectron-withdrawing anion, the counterion or cation of that salt may beany cation that allows the salt to revert or decompose back to the acidduring calcining. Factors that dictate the suitability of the particularsalt to serve as a source for the electron-withdrawing anion mayinclude, for example, the solubility of the salt in the desired solvent,the lack of adverse reactivity of the cation, ion-pairing effectsbetween the cation and anion, hygroscopic properties imparted to thesalt by the cation, and the like, and thermal stability of the anion.Examples of suitable cations in the salt of the electron-withdrawinganion include, for example, ammonium, trialkyl ammonium, tetraalkylammonium, tetraalkyl phosphonium, H⁺, [H(OEt₂)₂]⁺, and the like.

c. Examples of Processes to Produce a Chemically Treated Solid Oxide

Combinations of one or more different electron withdrawing anions, invarying proportions, may be used to tailor the specific acidity of theactivator-support to the desired level. Such combinations may becontacted with the oxide material simultaneously or individually, and inany order that affords the desired activator-support acidity. Forexample, the present techniques may employ two or moreelectron-withdrawing anion source compounds in two or more separatecontacting steps. Thus, one example of such a process by which anactivator-support may be prepared is as follows. A selected solid oxidecompound, or combination of oxide compounds, may be contacted with afirst electron-withdrawing anion source compound to form a first mixtureand this first mixture may be calcined. The calcined first mixture maybe contacted with a second electron-withdrawing anion source compound toform a second mixture. The second mixture may be calcined to form atreated solid oxide compound. In such a process, the first and secondelectron-withdrawing anion source compounds may be different compoundsor they may be the same compound.

The solid oxide activator-support may be produced by a process thatincludes contacting a solid oxide compound with an electron-withdrawinganion source compound to form a first mixture. The first mixture may bethen calcined to form the solid oxide activator-support.

Alternatively, the solid oxide activator-support may be produced by aprocess that includes contacting a solid oxide compound with a firstelectron-withdrawing anion source compound to form a first mixture. Thefirst mixture may be calcined, and then the calcined first mixture maybe contacted with a second electron-withdrawing anion source compound toform a second mixture. The second mixture may be calcined to form thesolid oxide activator-support. The solid oxide activator-support may bereferred to as a chemically treated solid oxide (CTSO) compound.

In another alternative, the solid oxide activator-support may beproduced by contacting a solid oxide with an electron-withdrawing anionsource compound. In this procedure the solid oxide compound may becalcined before, during or after contacting with theelectron-withdrawing anion source, and when there are aluminoxanes ororganoborates present.

Calcining of the treated solid oxides may be conducted in an ambient orinert atmosphere, typically in a dry ambient atmosphere, at atemperature from about 200° C. to about 900° C., and for a time of about1 minute to about 100 hours. Calcining may also be conducted at atemperature from about 300° C. to about 800° C., or from about 400° C.to about 700° C. Calcining may be conducted from about 1 hour to about50 hours, or from about 3 hours to about 20 hours. In embodiments,calcining may be carried out from about 1 to about 10 hours at atemperature from about 350° C. to about 550° C.

Further, calcining may typically be conducted in an ambient atmosphere,at an elevated temperature. Generally, calcining may be conducted in anoxidizing atmosphere, such as air. Alternatively, calcining may beperformed in an inert atmosphere, such as nitrogen or argon, or in areducing atmosphere such as hydrogen or carbon monoxide.

The solid oxide component used to prepare the chemically-treated solidoxide may have a pore volume greater than about 0.1 cc/g, a pore volumegreater than about 0.5 cc/g, or a pore volume greater than about 1.0cc/g. The solid oxide component may have a surface area from about 100to about 1000 m²/g, from about 200 to about 800 m²/g, or from about 250to about 600 m²/g.

d. Examples of Chemically Treated Solid Oxides

The solid oxide material may be treated with a source of halide ion orsulfate ion, or a combination of anions, and optionally treated with ametal ion, then calcined to provide the activator-support in the form ofa particulate solid. In one embodiment, the solid oxide material may betreated with a source of sulfate, termed a sulfating agent, a source ofchloride ion, termed a chloriding agent, a source of fluoride ion,termed a fluoriding agent, or a combination thereof, and calcined toprovide the solid oxide activator. Examples of useful acidicactivator-supports may include, for example: bromided alumina; chloridedalumina; fluorided alumina; sulfated alumina; bromided silica-alumina,chlorided silica-alumina; fluorided silica-alumina; sulfatedsilica-alumina; bromided silica-zirconia; chlorided silica-zirconia;fluorided silica-zirconia; sulfated silica-zirconia; chloridedzinc-alumina; triflate treated silica-alumina; a pillared clay, such asa pillared montmorillonite, optionally treated with fluoride, chloride,or sulfate; phosphated alumina, or other aluminophosphates, optionallytreated with sulfate, fluoride, or chloride; or any combination thereof.Further, any of the activator-supports may optionally be treated withanother metal ion, typically from a metal salt or compound, wherein themetal ion may be the same as or different from any metal that makes upthe solid oxide material.

The treated oxide activator-support may include a fluorided solid oxidein the form of a particulate solid, thus a source of fluoride ion may beadded to the oxide by treatment with a fluoriding agent. For example,fluoride ion may be added to the oxide by forming a slurry of the oxidein a suitable solvent such as alcohol or water, including, for example,alcohols having one to three carbon alcohols. Such alcohols may beselected due to their volatility and low surface tension. Examples offluoriding agents that may be used in the present techniques includehydrofluoric acid (HF), ammonium fluoride (NH₄F), ammonium bifluoride(NH₄HF₂), ammonium tetrafluorob orate (NH₄BF₄), ammonium silicofluoride(hexafluorosilicate) ((NH₄)₂SiF₆), ammonium hexafluorophosphate(NH₄PF₆), tetrafluoroboric acid (HBF₄), ammonium hexafluorotitanate(NH₄)₂TiF₆, ammonium hexafluorozirconate (NH₄)₂ZrF₆, analogs thereof,and combinations thereof. A specific fluoriding agent, ammoniumbifluoride NH₄HF₂, may often be used due to its ease of use and readyavailability.

The solid oxide may be treated with a fluoriding agent during thecalcining step. Any fluoriding agent capable of thoroughly contactingthe solid oxide during the calcining step may be used. For example, inaddition to those fluoriding agents described previously, volatileorganic fluoriding agents may be used. Such volatile organic fluoridingagents that may be used in embodiments include, for example, freons,perfluorohexane, perfluorobenzene, fluoromethane, trifluoroethanol, andcombinations thereof. Gaseous hydrogen fluoride or fluorine itself mayalso be used with the solid oxide if it is fluorided during calcining.One convenient method of contacting the solid oxide with the fluoridingagent may be to vaporize a fluoriding agent into a gas stream used tofluidize the solid oxide during calcination.

Similarly, the chemically-treated solid oxide may include a chloridedsolid oxide in the form of a particulate solid, thus a source ofchloride ion may be added to the oxide by treatment with a chloridingagent. The chloride ion may be added to the oxide by forming a slurry ofthe oxide in a suitable solvent. The solid oxide may also be treatedwith a chloriding agent during the calcining step. Any chloriding agentthat may be capable of serving as a source of chloride and thoroughlycontacting the oxide during the calcining step may be used. For example,volatile organic chloriding agents may be used. Examples of suchvolatile organic chloriding agents include, for example, certain freons,perchlorobenzene, chloromethane, dichloromethane, chloroform, carbontetrachloride, trichloroethanol, or any combination thereof. Gaseoushydrogen chloride or chlorine itself may also be used with the solidoxide during calcining. One convenient method of contacting the oxidewith the chloriding agent may be to vaporize a chloriding agent into agas stream used to fluidize the solid oxide during calcination.

e. Concentration of Electron-Withdrawing Anions

When the activator-support includes a chemically-treated solid oxideincluding a solid oxide treated with an electron-withdrawing anion, theelectron withdrawing anion may be added to the solid oxide in an amountgreater than about 1% by weight of the solid oxide. The electronwithdrawing anion may be added to the solid oxide in an amount greaterthan about 2% by weight of the solid oxide, greater than about 3% byweight of the solid oxide, greater than about 5% by weight of the solidoxide, or greater than about 7% by weight of the solid oxide.

The amount of electron-withdrawing ion, for example fluoride or chlorideion, present before calcining the solid oxide may be from about 2 toabout 50% by weight, where the weight percents are based on the weightof the solid oxide, for example silica-alumina, before calcining. Theamount of electron-withdrawing ion, for example fluoride or chlorideion, present before calcining the solid oxide may be from about 3 toabout 25% by weight or from about 4 to about 20% by weight.Alternatively, halide ion or may be used in an amount sufficient todeposit, after calcining, from about 0.1% to about 50%, from about 0.5%to about 40%, or from about 1% to about 30% by weight halide ionrelative to the weight of the solid oxide. If the fluoride or chlorideion is added during calcining, such as when calcined in the presence ofCCl₄, there may be typically no, or only trace levels, of fluoride orchloride ion in the solid oxide before calcining. Once impregnated withhalide, the halided oxide may be dried by any method. Such methods mayinclude, for example, suction filtration followed by evaporation, dryingunder vacuum, spray drying, and the like. It may also be possible toinitiate the calcining step immediately without drying the impregnatedsolid oxide.

The silica-alumina used to prepare the treated silica-alumina may have apore volume greater than about 0.5 cc/g. Alternatively, the pore volumemay be greater than about 0.8 cc/g, or greater than about 1.0 cc/g.Further, the silica-alumina may have a surface area greater than about100 m²/g, 250 m²/g, or 350 m²/g. Generally, the silica-alumina of thepresent techniques may have an alumina content from about 5 to about95%. Alternatively, the alumina content of the silica-alumina may befrom about 5 to about 50%, or from about 8% to about 30% alumina byweight.

The sulfated solid oxide may include sulfate and a solid oxide componentsuch as alumina or silica-alumina, in the form of a particulate solid.Optionally, the sulfated oxide may be further treated with a metal ionsuch that the calcined sulfated oxide may include a metal. For example,the sulfated solid oxide may include sulfate and alumina. The sulfatedalumina may be formed by a process wherein the alumina may be treatedwith a sulfate source, including, for example, sulfuric acid or asulfate salt such as ammonium sulfate, zinc sulfate, aluminum sulfate,nickel sulfate or copper sulfate, among others. This process may beperformed by forming a slurry of the alumina in a suitable solvent suchas alcohol or water, in which the desired concentration of the sulfatingagent has been added. Suitable organic solvents include, for example,the one to three carbon alcohols because of their volatility and lowsurface tension.

The amount of sulfate ion present before calcining may be from about 1%to about 50% by weight, from about 2% to about 30% by weight, or fromabout 5% to about 25% by weight, where the weight percents are based onthe weight of the solid oxide before calcining. Once impregnated withsulfate, the sulfated oxide may be dried by any method including, butnot limited to, suction filtration followed by evaporation, drying undervacuum, spray drying, and the like, although it may also be possible toinitiate the calcining step immediately.

In addition to being treated with an electron-withdrawing component suchas halide or sulfate ion, the solid inorganic oxide of the presenttechniques may be treated with a metal source, including metal salts ormetal-containing compounds. These compounds may be added to orimpregnated onto the solid oxide in solution form, and subsequentlyconverted into the supported metal upon calcining. Accordingly, thesolid inorganic oxide may further include zinc, nickel, vanadium,silver, copper, gallium, tin, tungsten, molybdenum, or a combinationthereof. For example, zinc may be used to impregnate the solid oxidebecause it provides good catalyst activity and low cost. The solid oxidemay be treated with metal salts or metal-containing compounds before,after, or at the same time that the solid oxide may be treated with theelectron-withdrawing anion.

Further, any method of impregnating the solid oxide material with ametal may be used. The method by which the oxide may be contacted with ametal source, typically a salt or metal-containing compound, mayinclude, for example, gelling, co-gelling, impregnation of one compoundonto another compound, and similar techniques. Following any contactingmethod, the contacted mixture of oxide compound, electron-withdrawinganion, and the metal ion may be calcined. Alternatively, a solid oxidematerial, an electron-withdrawing anion source, and the metal salt ormetal-containing compound may be contacted and calcined simultaneously.

The ansa-metallocene compound may be contacted with an olefin monomerand an organoaluminum cocatalyst for a first period of time prior tocontacting this mixture with an acidic activator-support. Once theprecontacted mixture of metallocene, monomer, and a component thatprovides an activatable ligand to the metallocene, e.g., anorganoaluminum cocatalyst, is contacted with the acidicactivator-support, the composition may be termed the “postcontacted”mixture. The postcontacted mixture may be allowed to remain in furthercontact for a second period of time prior to being charged into thereactor in which the polymerization process will be carried out.

Various processes to prepare solid oxide activator-supports that may beused in the present techniques have been reported. For example, U.S.Pat. Nos. 6,107,230, 6,165,929, 6,294,494, 6,300,271, 6,316,553,6,355,594, 6,376,415, 6,391,816, 6,395,666, 6,524,987, and 6,548,441,describe such methods, each of which is incorporated by referenceherein, in its entirety.

3. Ion-Exchangeable and Layered Mineral Activator-Supports

The activator-support of the present techniques may include clayminerals having exchangeable cations and layers capable of expanding.These activator supports include ion-exchangeable materials, such as,for example, silicate and aluminosilicate compounds or minerals, eitherwith layered or non-layered structures, and any combination thereof.Typical clay mineral activator-supports include layered aluminosilicatessuch as pillared clays. Although the term “support” may be used, it isnot meant to be construed as an inert component of the catalystcomposition, but rather may be considered an active part of the catalystcomposition, because of its intimate association with theansa-metallocene and the component that provides an activatable ligandto the metallocene, such as an organoaluminum. While not intending to bebound by theory, it is believed that the ion exchangeableactivator-support may serve as an insoluble reactant that reacts withthe ansa-metallocene and organoaluminum components to form a catalystcomposition used to produce polymer. When the acidic activator-supportincludes an ion-exchangeable activator-support, it may optionally betreated with an electron-withdrawing anion such as those discussedabove, though typically the ion-exchangeable activator-support is nottreated with an electron-withdrawing anion.

The clay materials of the present techniques may encompass materialseither in their natural state or that have been treated with variousions by wetting, ion exchange, or pillaring. The clay materialactivator-support of the present techniques may include clays that havebeen ion exchanged with large cations, including polynuclear, highlycharged metal complex cations. However, the clay materialactivator-supports of the present techniques also encompass clays thathave been ion exchanged with simple salts, including, but not limitedto, salts of Al(III), Fe(II), Fe(III) and Zn(II) with ligands such ashalide, acetate, sulfate, nitrate, or nitrite.

The clay activator-support of the present techniques may includepillared clays. The term pillared clays may be used to refer to claymaterials that have been ion exchanged with large, typicallypolynuclear, highly charged metal complex cations. Examples of such ionsinclude, for example, Keggin ions which may have charges such as 7+,various polyoxometallates, and other large ions. Thus, the termpillaring refers to a simple exchange reaction in which the exchangeablecations of a clay material may be replaced with large, highly chargedions, such as Keggin ions. These polymeric cations may then beimmobilized within the interlayers of the clay and when calcined areconverted to metal oxide “pillars,” effectively supporting the claylayers as column-like structures. Thus, once the clay is dried andcalcined to produce the supporting pillars between clay layers, theexpanded lattice structure may be maintained, enhancing the porosity.The resulting pores can vary in shape and size as a function of thepillaring material and the parent clay material used. Examples ofpillaring and pillared clays may be found in U.S. Pat. Nos. 4,452,910,5,376,611, and 4,060,480, each of which is incorporated herein in itsentirety.

The pillaring process utilizes clay minerals having exchangeable cationsand layers capable of expanding. Any pillared clay that can enhance thepolymerization of olefins in the catalyst composition of the presenttechniques may be used. Therefore, suitable clay minerals for pillaringmay include, for example: allophanes; smectites, including dioctahedral(Al) and tri-octahedral (Mg) smectites and derivatives thereof, such asmontmorillonites (bentonites), nontronites, hectorites, or laponites;halloysites; vermiculites; micas; fluoromicas; chlorites; mixed-layerclays; the fiberous clays such as sepiolites and attapulgites(palygorskites); serpentine clays; illite; laponite; saponite; or anycombination thereof. In one embodiment, the pillared clayactivator-support may include bentonite or montmorillonite, noting thatthe principal component of bentonite is montmorillonite.

The ion-exchangeable activator-supports such as pillared clays used toprepare the catalyst compositions of the present techniques may becombined with other inorganic support materials, including, for example,zeolites, inorganic oxides, phosphated inorganic oxides, and the like.In embodiments, typical support materials that may be used in thisregard include, for example, silica, silica-alumina, alumina, titania,zirconia, magnesia, boria, fluorided alumina, silated alumina, thoria,aluminophosphate, aluminum phosphate, zinc aluminate, phosphated silica,phosphated alumina, silica-titania, coprecipitated silica/titania,fluorided/silated alumina, and any combination or mixture thereof. Theamount of ansa-metallocene compound in relation to the ion-exchangableactivator-support used to prepare the catalyst composition of thepresent techniques may be from about 0.1 wt % to about 15 wt %ansa-metallocene complex, based on the weight of the activator-supportcomponent (not based on the final metallocene-clay mixture), or fromabout 1 wt % to about 10 wt % ansa-metallocene.

The mixture of ansa-metallocene and clay activator-support may becontacted and mixed for any length of time sufficient to allow thoroughinteraction between the ansa-metallocene and activator-support.Sufficient deposition of the metallocene component on the clay may beachieved without heating a mixture of clay and metallocene complex. Forexample, the ansa-metallocene compound and the clay material may besimply mixed at a temperature range from about room temperature to about200° F. in order to achieve the deposition of the ansa-metallocene onthe clay activator-support. Alternatively, the ansa-metallocene compoundand the clay material may be mixed from about 100° F. to about 180° F.in order to achieve the deposition of the ansa-metallocene on the clayactivator-support.

The present techniques encompass catalyst compositions including anacidic activator-support, which may include a layered mineral. The term“layered mineral” is used herein to describe materials such as clayminerals, pillared clays, ion-exchanged clays, exfoliated clays,exfoliated clays gelled into another oxide matrix, layered mineralsmixed or diluted with other materials, and the like, or any combinationthereof. When the acidic activator-support includes a layered mineral,it may optionally be treated with an electron-withdrawing anion such asthose presented herein, though typically the layered mineral may not betreated with an electron-withdrawing anion. For example, a clay mineralmay be used as the activator-support.

Clay minerals generally include the large group of finely-crystalline,sheet-like layered minerals that are found in nature in fine-grainedsediments, sedimentary rocks, and the like, and which constitute a classof hydrous silicate and aluminosilicate minerals with sheet-likestructures and very high surface areas. This term may also be used todescribe hydrous magnesium silicates with a phyllosilicate structure.Examples of clay minerals that may be used in the present techniquesinclude, for example, allophanes; smectites, including dioctahedral (Al)and tri-octahedral (Mg) smectities and derivatives thereof such asmontmorillonites (bentonites), nontronites, hectorites, or laponites;halloysites; vermiculites; micas; fluoromicas; chlorites; mixed-layerclays; the fiberous clays, such as sepiolites and attapulgites(palygorskites); a serpentine clay; illite; laponite; saponite; or anycombination thereof. Many common clay minerals belong to the kaolinite,montmorillonite, or illite groups of clays.

When layered minerals are used as activator-supports or metalloceneactivators, the layered minerals may be calcined prior to their use asactivators. Typical calcination temperatures may range from about 100°C. to about 700° C., from about 150° C. to about 500° C., or from about200° C. to about 400° C.

4. Organoaluminoxane Activators/Cocatalysts

The present techniques may include catalyst compositions that useorganoaluminoxane compounds as activators and/or cocatalysts. Thecatalyst composition may not require an acidic activator-support such asa chemically-treated solid oxide to weaken the bonds between the metaland the X³ or X⁴ ligands, as the organoaluminoxane may perform thisfunction, or may replace the X³ or X⁴ ligands with more active species.The catalyst composition may also not require an organoaluminumcompound. Thus, any ansa-metallocene compounds presented herein may becombined with any of the aluminoxanes presented herein, or anycombination of aluminoxanes presented herein, to form catalystcompositions of the present techniques. Further, any ansa-metallocenecompounds presented herein may be combined with any aluminoxane orcombination of aluminoxanes, and optionally an activator-support suchas, for example, a layered mineral, an ion-exchangeableactivator-support, an organoboron compound or an organoborate compound,to form a catalyst composition of the present techniques.

Aluminoxanes may be referred to as poly(hydrocarbyl aluminum oxides) ororganoaluminoxanes. The other catalyst components may be contacted withthe aluminoxane in a saturated hydrocarbon compound solvent, though anysolvent which is substantially inert to the reactants, intermediates,and products of the activation step may be used. The catalystcomposition formed in this manner may be collected by any methodincluding, but not limited to filtration, or the catalyst compositionmay be introduced into the polymerization reactor without beingisolated.

The aluminoxane compound of the present techniques may be an oligomericaluminum compound, wherein the aluminoxane compound may include linearstructures, cyclic, or cage structures, or mixtures of all three. Cyclicaluminoxane compounds having the formula:

whereinR may be a linear or branched alkyl having from 1 to 10 carbon atoms,and n may be an integer from 3 to about 10 may be encompassed by thepresent techniques. The (AlRO)_(n) moiety shown here also constitutesthe repeating unit in a linear aluminoxane. Thus, linear aluminoxaneshaving the formula:

whereinR may be a linear or branched alkyl having from 1 to 10 carbon atoms,and n may be an integer from 1 to about 50, are also encompassed by thepresent techniques.

Further, useful aluminoxanes may also have cage structures of theformula R^(t) _(5m+α)R^(b) _(m−α)Al_(4m)O_(3m), wherein m may be 3 or 4and a is equal to n_(Al(3))−n_(O(2))+n_(O(4)). In this structuren_(Al(3)) is the number of three coordinate aluminum atoms, n_(O(2)) isthe number of two coordinate oxygen atoms, and n_(O(4)) is the number of4 coordinate oxygen atoms. R^(t) represents a terminal alkyl group andR^(b) represents a bridging alkyl group, either of which may have from 1to 10 carbon atoms.

Thus, aluminoxanes may be represented generally by formulas such as(R—Al—O)_(n), R(R—Al—O)_(n)AlR₂, and the like, wherein the R group maybe a linear or branched C₁-C₆ alkyl such as methyl, ethyl, propyl,butyl, pentyl, or hexyl, and n may represent an integer from 1 to about50. The aluminoxane compounds of the present techniques may include, forexample, methylaluminoxane, ethylaluminoxane, n-propylaluminoxane,iso-propylaluminoxane, n-butylaluminoxane, t-butylaluminoxane,sec-butylaluminoxane, iso-butylaluminoxane, 1-pentylaluminoxane,2-pentylaluminoxane, 3-pentylaluminoxane, iso-pentylaluminoxane,neopentylaluminoxane, or combinations thereof.

While organoaluminoxanes with different types of R groups areencompassed by the present techniques, methyl aluminoxane (MAO), ethylaluminoxane, or isobutyl aluminoxane may also be used as cocatalysts inthe compositions of the present techniques. These aluminoxanes may beprepared from trimethylaluminum, triethylaluminum, ortriisobutylaluminum, respectively, and may be referred to as poly(methylaluminum oxide), poly(ethyl aluminum oxide), and poly(isobutyl aluminumoxide), respectively. It is also within the scope of the currenttechniques to use an aluminoxane in combination with a trialkylaluminum,such as disclosed in U.S. Pat. No. 4,794,096, which is hereinincorporated by reference in its entirety.

The present techniques encompasses many values of n in the aluminoxaneformulas (R—Al—O)_(n) and R(R—Al—O)_(n)AlR₂. In exemplary aluminoxanes,n may be at least about 3. However, depending upon how theorganoaluminoxane may be prepared, stored, and used, the value of n maybe variable within a single sample of aluminoxane, and such combinationsof organoaluminoxanes are encompassed by the methods and compositions ofthe present techniques.

In embodiments of the present techniques that include the optionalaluminoxane, the molar ratio of the aluminum in the aluminoxane to themetallocene in the composition may be from about 1:10 to about100,000:1, or from about 5:1 to about 15,000:1. The amount of optionalaluminoxane added to a polymerization zone may be an amount within arange of about 0.01 mg/L to about 1000 mg/L, from about 0.1 mg/L toabout 100 mg/L, or from about 1 mg/L to about 50 mg/L.

Organoaluminoxanes may be prepared by various procedures which areavailable. Examples of organoaluminoxane preparations are disclosed inU.S. Pat. Nos. 3,242,099 and 4,808,561, each of which is incorporated byreference herein, in its entirety. One example of how an aluminoxane maybe prepared is as follows. Water may be dissolved in an inert organicsolvent and then reacted with an aluminum alkyl compound such as AlR₃ toform the desired organoaluminoxane compound. While not intending to bebound by this statement, it is believed that this synthetic method canafford a mixture of both linear and cyclic (R—Al—O)_(n) aluminoxanespecies, both of which are encompassed by the present techniques.Alternatively, organoaluminoxanes may be prepared by reacting analuminum alkyl compound such as AlR₃ with a hydrated salt, such ashydrated copper sulfate, in an inert organic solvent.

5. Organoboron and Organoborate Activators/Cocatalysts

The present techniques also encompass catalyst compositions that useorganoboron or organoborate compounds as activators and/or cocatalysts.Any ansa-metallocene compound presented herein may be combined with anyof the organoboron or organoborate cocatalysts presented herein, or anycombination of organoboron or organoborate cocatalysts presented herein.This composition may include a component that provides an activatableligand such as an alkyl or hydride ligand to the metallocene, when themetallocene compound does not already include such a ligand, such as anorganoaluminum compound. Further, any ansa-metallocene compoundspresented herein may be combined with: any an organoboron ororganoborate cocatalyst; an organoaluminum compound; optionally, analuminoxane; and optionally, an activator-support; to form a catalystcomposition of the present techniques.

The term “organoboron” compound may be used to refer to neutral boroncompounds, borate salts, or combinations thereof. For example, theorganoboron compounds in various embodiments may be a fluoroorgano boroncompound, a fluoroorgano borate compound, or a combination thereof. Anyfluoroorgano boron or fluoroorgano borate compound may be utilized. Theterm fluoroorgano boron has its usual meaning to refer to neutralcompounds of the form BY₃. The term fluoroorgano borate compound alsohas its usual meaning to refer to the monoanionic salts of afluoroorgano boron compound of the form [cation]⁺[BY₄]⁻, where Yrepresents a fluorinated organic group. For convenience, fluoroorganoboron and fluoroorgano borate compounds may be referred to collectivelyby organoboron compounds, or by either name as the context requires.

Fluoroorgano borate compounds that may be used as cocatalysts in thepresent techniques include, for example, fluorinated aryl borates suchas, N,N-dimethylanilinium tetrakis-(pentafluorophenyl)-borate,triphenylcarbenium tetrakis(pentafluorophenyl)borate, lithiumtetrakis-(pentafluorophenyl)borate, N,N-dimethylaniliniumtetrakis[3,5-bis(trifluoro-methyl)phenyl]borate, triphenylcarbeniumtetrakis[3,5-bis(trifluoromethyl)-phenyl]borate, and the like, includingmixtures thereof. Examples of fluoroorgano boron compounds that may beused as cocatalysts in the present techniques include, for example,tris(pentafluorophenyl)boron,tris[3,5-bis(trifluoromethyl)-phenyl]boron, and the like, includingmixtures thereof.

Although not intending to be bound by the following theory, theseexamples of fluoroorgano borate and fluoroorgano boron compounds, andrelated compounds, are thought to form “weakly-coordinating” anions whencombined with organometal compounds, as disclosed in U.S. Pat. No.5,919,983, which is herein included by reference in its entirety herein.

Generally, any amount of organoboron compound may be utilized in thepresent techniques. In some embodiments, the molar ratio of theorganoboron compound to the metallocene compound in the composition maybe from about 0.1:1 to about 10:1, or from about 0.5 mole to about 10moles of boron compound per mole of metallocene compound. Inembodiments, the amount of fluoroorgano boron or fluoroorgano boratecompound used as a cocatalyst for the metallocene may range of fromabout 0.8 mole to about 5 moles of boron compound per mole ofmetallocene compound.

6. Ionizing Ionic Compound Activators/Cocatalysts

Embodiments of the present techniques may include a catalyst compositionas presented herein, including an optional ionizing ionic compound as anactivator and/or cocatalyst in addition to other components. Examples ofionizing ionic compound are disclosed in U.S. Pat. Nos. 5,576,259 and5,807,938 which are herein incorporated by reference in their entirety.

An ionizing ionic compound is an ionic compound which can function toenhance activity of the catalyst composition. While not intending to bebound by theory, it is believed that the ionizing ionic compound may becapable of reacting with the metallocene compound and converting themetallocene into a cationic metallocene compound. Again, while notintending to be bound by theory, it is believed that the ionizing ioniccompound can function as an ionizing compound by completely or partiallyextracting an anionic ligand, possibly a non-η⁵-alkadienyl ligand, suchas X³ or X⁴, from the metallocene. However, the ionizing ionic compoundis an activator regardless of whether it is ionizes the metallocene,abstracts an X³ or X⁴ ligand in a fashion as to form an ion pair,weakens the metal-(X³) or metal-(X⁴) bond in the metallocene, simplycoordinates to an X³ or X⁴ ligand, or follows any other mechanisms bywhich activation can occur. Further, it is not necessary that theionizing ionic compound activate the metallocene only. The activationfunction of the ionizing ionic compound may be evident in the enhancedactivity of catalyst composition as a whole, as compared to a catalystcomposition containing catalyst composition that does not include anyionizing ionic compound.

Examples of ionizing ionic compounds may include, for example, suchcompounds as: tri(n-butyl)ammonium tetrakis(p-tolyl)borate,tri(n-butyl)-ammonium tetrakis(m-tolyl)borate, tri(n-butyl)ammoniumtetrakis(2,4-dimethylphenyl)-borate, tri(n-butyl)ammoniumtetrakis(3,5-dimethylphenyl)borate, tri(n-butyl)-ammoniumtetrakis[3,5-bis(trifluoro-methyl)phenyl]borate, tri(n-butyl)ammoniumtetrakis(pentafluorophenyl)borate, N,N-dimethylaniliniumtetrakis(p-tolyl)borate, N,N-dimethylanilinium tetrakis(m-tolyl)borate,N,N-dimethylanilinium tetrakis(2,4-dimethylphenyl)borate,N,N-dimethylanilinium tetrakis(3,5-dimethyl-phenyl)borate,N,N-dimethylanilinium tetrakis[3,5-bis(trifluoro-methyl)phenyl]borate,N,N-dimethylanilinium tetrakis-(pentafluorophenyl)borate,triphenyl-carbenium tetrakis(p-tolyl)borate, triphenylcarbeniumtetrakis(m-tolyl)borate, triphenylcarbeniumtetrakis(2,4-dimethylphenyl)borate, triphenylcarbeniumtetrakis-(3,5-dimethylphenyl)borate, triphenylcarbeniumtetrakis[3,5-bis(trifluoro-methyl)phenyl]borate, triphenylcarbeniumtetrakis(pentafluorophenyl)borate, tropylium tetrakis(p-tolyl)borate,tropylium tetrakis(m-tolyl)borate, tropyliumtetrakis(2,4-dimethylphenyl)borate, tropyliumtetrakis(3,5-dimethylphenyl)borate, tropyliumtetrakis[3,5-bis(trifluoro-methyl)phenyl]-borate, tropyliumtetrakis(pentafluorophenyl)borate, lithiumtetrakis(pentafluorophenyl)-borate, lithium tetrakis(phenyl)borate,lithium tetrakis(p-tolyl)borate, lithium tetrakis(m-tolyl)borate,lithium tetrakis(2,4-dimethylphenyl)borate, lithiumtetrakis-(3,5-dimethylphenyl)borate, lithium tetrafluoroborate, sodiumtetrakis(pentafluoro-phenyl)borate, sodium tetrakis(phenyl) borate,sodium tetrakis(p-tolyl)borate, sodium tetrakis(m-tolyl)borate, sodiumtetrakis(2,4-dimethylphenyl)borate, sodiumtetrakis-(3,5-dimethylphenyl)borate, sodium tetrafluoroborate, potassiumtetrakis-(pentafluorophenyl)borate, potassium tetrakis(phenyl)borate,potassium tetrakis(p-tolyl)borate, potassium tetrakis(m-tolyl)borate,potassium tetrakis(2,4-dimethyl-phenyl)borate, potassiumtetrakis(3,5-dimethylphenyl)borate, potassium tetrafluoro-borate,triphenylcarbenium tetrakis(p-tolyl)aluminate, triphenylcarbeniumtetrakis(m-tolyl)-aluminate, triphenylcarbeniumtetrakis(2,4-dimethylphenyl)aluminate, triphenyl-carbeniumtetrakis(3,5-dimethylphenyl)aluminate, triphenylcarbeniumtetrakis-(pentafluorophenyl)aluminate, tropyliumtetrakis(p-tolyl)aluminate, tropylium tetrakis(m-tolyl)aluminate,tropylium tetrakis(2,4-dimethylphenyl)aluminate, tropyliumtetrakis(3,5-dimethylphenyl)aluminate, tropyliumtetrakis(pentafluoro-phenyl)aluminate, lithiumtetrakis(pentafluorophenyl)aluminate, lithiumtetrakis-(phenyl)aluminate, lithium tetrakis(p-tolyl)aluminate, lithiumtetrakis(m-tolyl)aluminate, lithiumtetrakis(2,4-dimethylphenyl)aluminate, lithiumtetrakis(3,5-dimethylphenyl)aluminate, lithium tetrafluoroaluminate,sodium tetrakis(pentafluoro-phenyl)aluminate, sodiumtetrakis(phenyl)aluminate, sodium tetrakis(p-tolyl)-aluminate, sodiumtetrakis(m-tolyl)aluminate, sodiumtetrakis(2,4-dimethylphenyl)-aluminate, sodiumtetrakis(3,5-dimethylphenyl)aluminate, sodium tetrafluoroaluminate,potassium tetrakis(pentafluorophenyl)aluminate, potassiumtetrakis-(phenyl)aluminate, potassium tetrakis(p-tolyl)aluminate,potassium tetrakis(m-tolyl)-aluminate, potassiumtetrakis(2,4-dimethylphenyl)aluminate, potassium tetrakis(3,5-dimethylphenyl)aluminate, potassium tetrafluoroaluminate,triphenylcarbenium tris(2,2′,2″-nonafluorobiphenyl)fluoroaluminate,silver tetrakis(1,1,1,3,3,3-hexafluoro-isopropanolato)aluminate, orsilver tetrakis(perfluoro-t-butoxy)aluminate, or any combinationthereof.

D. Non-Limiting Examples of the Catalyst Composition

Exemplary catalyst compositions of the present techniques may includethe compositions described below. In embodiments, for example, thecatalyst composition may include, or the catalyst composition mayinclude the contact product of, an ansa-metallocene, an organoaluminumcompound, and an activator-support. The ansa-metallocene may includecompounds having the general formula:

In this formula, M¹ may be zirconium or hafnium and X′ and X″ may beindependently F, Cl, Br, or I. E may be C or Si and n may be an integerfrom 1 to 3 inclusive. R^(3A) and R^(3B) may be independently ahydrocarbyl group or a trihydrocarbylsilyl group, any of which may haveup to 20 carbon atoms, or may be hydrogen. The subscript ‘m’ may be aninteger that may range from 0 to 10, inclusive. R^(4A) and R^(4B) may beindependently a hydrocarbyl group that may have up to 12 carbon atoms,or may be hydrogen. Bond ‘a’ may be a single or a double bond. Theorganoaluminum compound may be, for example, trimethylaluminum,triethylaluminum, tripropylaluminum, tributylaluminum,triisobutylaluminum, trihexylaluminum, triisohexylaluminum,trioctylaluminum, diethylaluminum ethoxide, diisobutylaluminum hydride,diethylaluminum chloride, or any combination thereof. In thisembodiment, the activator-support may be a solid oxide treated with anelectron-withdrawing anion, wherein the solid oxide may be, for example,silica, alumina, silica-alumina, aluminophosphate, aluminum phosphate,zinc aluminate, heteropolytungstates, titania, zirconia, magnesia,boria, zinc oxide, mixed oxides thereof, or any combination thereof. Theelectron-withdrawing anion may be, for example, fluoride, chloride,bromide, iodide, phosphate, triflate, bisulfate, sulfate, fluoroborate,fluorosulfate, trifluoroacetate, phosphate, fluorophosphate,fluorozirconate, fluorosilicate, fluorotitanate, permanganate,substituted or unsubstituted alkanesulfonate, substituted orunsubstituted arenesulfonate, substituted or unsubstituted alkylsulfate,or any combination thereof.

In the embodiments described above, the ansa-metallocene may be acompound having the general formula:

In this formula, M¹ may be zirconium or hafnium, and X′ and X″ may beindependently F, Cl, Br, or I. E may be C or Si and ‘n’ may be aninteger from 1 to 3, inclusive. R^(3A) and R^(3B) may be independentlyH, methyl, ethyl, propyl, allyl, benzyl, butyl, pentyl, hexyl, ortrimethylsilyl, and ‘m’ may be an integer from 1 to 6, inclusive. R^(4A)and R^(4B) may be independently a hydrocarbyl group having up to 6carbon atoms, or hydrogen. Bond ‘a’ may be a single or a double bond.

In the embodiments described above, the ansa-metallocene may be acompound having the general formula:

In this formula, M¹ may be zirconium or hafnium, and X′ and X″ may beindependently F, Cl, Br, or I. E may be C or Si and ‘n’ may be 1 or 2.R^(3A) and R^(3B) may be independently H or methyl, and ‘m’ may be 1 or2. R^(4A) and R^(4B) may be independently H or t-butyl. Bond ‘a’ may bea single or a double bond.

In the embodiments described above, the ansa-metallocene of the presenttechniques may be a compound having the formula:

In this formula, M¹ may be zirconium or hafnium, and X′ and X″ may beindependently H, BH₄, methyl, phenyl, benzyl, neopentyl,trimethylsilylmethyl, CH₂CMe₂Ph; CH₂SiMe₂Ph; CH₂CMe₂CH₂Ph; orCH₂SiMe₂CH₂Ph. E may be C or Si and n may be an integer from 1 to 3,inclusive. R^(3A) and R^(3B) may be independently a hydrocarbyl group ora trihydrocarbylsilyl group, any of which having up to 20 carbon atoms,or hydrogen, and n may be an integer from 0 to 10, inclusive. R^(4A) andR^(4B) may be independently a hydrocarbyl group having up to 12 carbonatoms, or hydrogen. Bond ‘a’ may be a single or a double bond. In otherversions of the embodiments described above, the ansa-metallocene mayinclude compounds (I-1) or (I-2), as shown in FIG. 1, or any combinationthereof.

In other embodiments, the catalyst composition may include, or thecatalyst composition may include the contact product of, anansa-metallocene, an organoaluminum compound, and an activator-support.In this embodiment the ansa-metallocene may include compounds (I-1) or(I-2), as shown in FIG. 1, or any combination thereof. Theorganoaluminum compound may include triethylaluminum,tri-n-butylaluminum, triisobutylaluminum, or any combination thereof.The activator-support may include a sulfated solid oxide.

In still other embodiments, the catalyst composition may include, or thecatalyst composition may include the contact product of, anansa-metallocene, an organoaluminum compound, and an activator-support.In these embodiments the ansa-metallocene may include compounds (I-1) or(I-2), as shown in FIG. 1, or any combination thereof. Theorganoaluminum compound may include triethylaluminum,tri-n-butylaluminum, triisobutylaluminum, or any combination thereof.The activator-support may include sulfated alumina.

In still other embodiments, the catalyst composition may include, or thecatalyst composition may include the contact product of, a precontactedansa-metallocene, a precontacted organoaluminum compound, a precontactedolefin, and a postcontacted activator-support, wherein each of theansa-metallocene, the organoaluminum compound, the olefin, and theactivator-support may be as presented herein.

Further embodiments of the present techniques provide a catalystcomposition that includes the contact product of a tightly-bridgedansa-metallocene compound containing a cyclic bridging moiety attachedto both η5-cyclopentadienyl-type ligands, and a reagent that canfunction to convert the metallocene into an active catalyst that may bedifferent from the combination of the solid oxide activator-support andorganoaluminum compound presented herein. Thus, in one embodiment, theactive catalyst composition may be formed by activating the metallocene,which may include converting the metallocene compound to its cationicform, and by providing it with a hydrocarbyl ligand (e.g., alkylation)before, after, or during its conversion to a cation that can initiateolefin polymerization. The reagent that can convert the metallocene intoan active catalyst may include a component that provides an activatableligand such as an alkyl to the metallocene, when the metallocenecompound does not already include such a ligand, and an activatorcomponent, as provided herein. In some instances, both functions may beachieved with one component, for example, an organoaluminoxane. In otherinstances, these two functions may be provided by two separatecomponents, such as an organoaluminum compound that can provide anactivatable alkyl ligand to the metallocene, and another component thatcan provide the activator function.

The activator and/or alkylation agent for the ansa-metallocene compoundmay be an organoaluminoxane, such as, for example, methylaluminoxane orisobutylaluminoxane. Alternatively, the activator may be a Lewis acidicorganoboron compound capable of abstracting an anionic ligand from themetallocene, such as, for example, tris(pentafluorophenyl)boron ortriphenylcarbenium tetrakis(pentafluorophenyl)borate, that may be usedin combination with an alkylating agent such as an organoaluminumcompound.

Further, a dialkylated tightly-bridged ansa-metallocene compound aspresented herein may be reacted with a Brønsted acidic borate activatorsuch as tri(n-butyl)ammonium tetrakis(p-tolyl)borate orN,N-dimethylanilinium tetrakis-(pentafluorophenyl)borate to remove onealkyl ligand to form an alkylated metallocene cation. Alternatively, thedialkylated tightly-bridged ansa-metallocene compound may be reactedwith a Lewis acid borate activator such as triphenylcarbeniumtetrakis(pentafluorophenyl)borate to remove one alkyl ligand to form analkylated metallocene cation. Thus, while not intending to be bound bytheory, it is believed that the active catalyst may include an alkylatedmetallocene cation, and any number of alternate reactions may be used togenerate such a catalyst.

The present techniques may include a catalyst composition that containsa contact product of a tightly-bridged ansa-metallocene which includes ahydrocarbyl ligand that can initiate olefin polymerization and a solidoxide activator-support, without the need for the addition of anorganoaluminum compound. The ansa-metallocene compound may include apendant alkyl group attached to one of the η⁵-cyclopentadienyl-typeligand, and a hydrocarbyl ligand that can initiate olefinpolymerization. An organoaluminum compound may not be required toalkylate this type of “pre-alkylated” ansa-metallocene because italready includes a hydrocarbyl ligand that can initiate olefinpolymerization.

E. The Olefin Monomer

In the present techniques, various unsaturated reactants may be usefulin the polymerization processes with catalyst compositions andprocesses. Such reactants include olefin compounds having from about 2to about 30 carbon atoms per molecule and having an olefinic doublebond. The present techniques encompass homopolymerization processesusing a single olefin such as ethylene or propylene, as well ascopolymerization reactions with two or more different olefiniccompounds. For example, in a copolymerization reaction with ethylene,copolymers may include a major amount of ethylene (>50 mole percent) anda minor amount of comonomer <50 mole percent. The comonomers that may becopolymerized with ethylene may have from three to about 20 carbon atomsin their molecular chain.

Olefins that may be used as monomer or comonomer in the presenttechniques include acyclic, cyclic, polycyclic, terminal (cc), internal,linear, branched, substituted, unsubstituted, functionalized, andnon-functionalized olefins. For example, compounds that may bepolymerized with the catalysts of the present techniques includepropylene, 1-butene, 2-butene, 3-methyl-1-butene, isobutylene,1-pentene, 2-pentene, 3-methyl-1-pentene, 4-methyl-1-pentene, 1-hexene,2-hexene, 3-hexene, 3-ethyl-1-hexene, 1-heptene, 2-heptene, 3-heptene,the four normal octenes, the four normal nonenes, the five normaldecenes, or any combination thereof. Further, cyclic and bicyclicolefins, including, for example, cyclopentene, cyclohexene,norbornylene, norbornadiene, and the like, may also be polymerized asdescribed above.

The amount of comonomer introduced into a reactor zone to produce acopolymer may be from about 0.001 to about 99 weight percent comonomerbased on the total weight of the monomer and comonomer, generally fromabout 0.01 to about 50 weight percent. In other embodiments, the amountof comonomer introduced into a reactor zone may be from about 0.01 toabout 10 weight percent comonomer or from about 0.1 to about 5 weightpercent comonomer. Alternatively, an amount sufficient to give the abovedescribed concentrations, by weight, of the copolymer produced, may beused.

While not intending to be bound by theory, it is believed that sterichindrance can impede or slow the polymerization process if branched,substituted, or functionalized olefins are used as reactants. However,if the branched and/or cyclic portion(s) of the olefin are somewhatremoved from the carbon-carbon double bond they would not be expected tohinder the reaction as much as more proximate substituents.

In an exemplary embodiment, a reactant for the catalyst compositions ofthe present techniques may be ethylene, so the polymerizations may beeither homopolymerizations or copolymerizations with a differentacyclic, cyclic, terminal, internal, linear, branched, substituted, orunsubstituted olefin. In addition, the catalyst compositions of thepresent techniques may be used in polymerization of diolefin compounds,including for example, such compounds as 1,3-butadiene, isoprene,1,4-pentadiene, and 1,5-hexadiene.

II. Preparation of the Catalyst Composition

The present techniques encompass a catalyst composition and a methodthat includes contacting a tightly-bridged ansa-metallocene compound, anactivator, and optionally an organoaluminum compound, as presentedherein. The method presented herein encompasses any series of contactingsteps that allows contacting each of the components including any orderof contacting components or mixtures of components. While not intendingto be limiting, examples of contacting steps may be exemplified using atreated solid oxide activator-support and an organoaluminum cocatalyst.These steps may encompass any number of precontacting and postcontactingsteps, and may further encompass using an olefin monomer as a contactcomponent in any of these steps. Examples of methods to prepare thecatalyst composition of the present techniques are discussed below.

A. Precontacting the Catalyst Composition with an Olefin

Precontacting a catalyst composition, or a component of a catalystcomposition, with an olefinic monomer prior to adding the catalystcomposition to a reactor may increase the productivity of the polymer ascompared to the same catalyst composition that may be prepared without aprecontacting step. The enhanced activity catalyst composition of thepresent techniques may be used for homopolymerization of an α-olefinmonomer such as ethylene or copolymerization of an α-olefin and acomonomer. However, a precontacting step is not required in the catalystcompositions of the present techniques.

In some embodiments of the present techniques, the ansa-metallocene maybe precontacted with an olefinic monomer, although not necessarily theolefin monomer to be polymerized, and an organoaluminum cocatalyst for afirst period of time. This precontacted mixture may then be contactedwith the solid oxide activator-support. For example, the first period oftime for contact, the precontact time, between the ansa-metallocene, theolefinic monomer, and the organoaluminum cocatalyst may range in timefrom about 1 minute to about 24 hours, from about 0.1 to about 1 hour,or from about 10 minutes to about 30 minutes.

Once the precontacted mixture of ansa-metallocene, olefin monomer, andorganoaluminum cocatalyst is contacted with the solid oxide activator,this composition (further including the solid oxide activator) may betermed the postcontacted mixture. The postcontacted mixture may beallowed to remain in contact for a second period of time, thepostcontact time, prior to being used in the polymerization process.This may provide increases in activity in a similar fashion toprecontacting the catalyst composition. Postcontact times between thesolid oxide activator-support and the precontacted mixture may range intime from about 1 minute to about 24 hours, from 0.1 hours to about 1hour, or from about 10 minutes to about 30 minutes.

The various catalyst components (for example, ansa-metallocene,activator-support, organoaluminum cocatalyst, and optionally anunsaturated hydrocarbon) may be contacted in the polymerization reactorsimultaneously while the polymerization reaction is proceeding.Alternatively, any two or more of these catalyst components may beprecontacted in a vessel or tube prior to their entering the reactionzone. This precontacting step may be a continuous process, in which theprecontacted product may be fed continuously to the reactor, or it maybe a stepwise or batchwise process in which a batch of precontactedproduct may be added to make a catalyst composition. This precontactingstep may be carried out over a time period that may range from a fewseconds to as much as several days, or longer. For example, thecontinuous precontacting step may last from about 1 second to about 1hour, from about 10 seconds to about 45 minutes, or from about 1 minuteto about 30 minutes.

B. Multiple Precontacting Steps

Alternatively the precontacting process may be carried out in multiplesteps, rather than a single step, in which multiple mixtures areprepared, each including a different set of catalyst components. Forexample, at least two catalyst components may be contacted forming afirst mixture, followed by contacting the first mixture with anothercatalyst component forming a second mixture, and so forth.

Multiple precontacting steps may be carried out in a single vessel or inmultiple vessels. Further, multiple precontacting steps may be carriedout in series (sequentially), in parallel, or a combination thereof. Forexample, a first mixture of two catalyst components may be formed in afirst vessel, a second mixture including the first mixture plus oneadditional catalyst component may be formed in the first vessel or in asecond vessel, which may be placed downstream of the first vessel.

One or more of the catalyst components may be split and used indifferent precontacting treatments. For example, part of a catalystcomponent may be fed into a first precontacting vessel for precontactingwith another catalyst component, while the remainder of that samecatalyst component may be fed into a second precontacting vessel forprecontacting with another catalyst component, or may be fed directlyinto the reactor, or a combination thereof. The precontacting may becarried out in any suitable equipment, such as tanks, stirred mix tanks,various static mixing devices, a tube, a flask, a vessel of any type, orany combination thereof. For example, a catalyst composition of thepresent techniques may be prepared by contacting 1-hexene,triisobutylaluminum or tri-n-butylaluminum, and an ansa-metallocene forat least about 30 minutes, followed by contacting the precontactedmixture with a sulfated alumina activator-support for at least about 10minutes up to one hour to form the active catalyst.

The postcontacted mixture may be heated at a temperature and for a timesufficient to allow adsorption, impregnation, or interaction ofprecontacted mixture and the solid oxide activator-support, such that aportion of the components of the precontacted mixture may beimmobilized, adsorbed, or deposited thereon. For example, thepostcontacted mixture may be heated from between about 0° F. to about150° F., or from between about 40° F. to about 95° F. Neither aprecontacting step nor a postcontacting step may be required for thepresent techniques.

C. Composition Ratios for Catalyst Compositions

In embodiments of the present techniques, the molar ratio of theansa-metallocene compound to the organoaluminum compound may be fromabout 1:1 to about 1:10,000 (e.g., about 1:2, 1:5, 1:20, 1:50, 1:200,1:500, 1:2000, 1:5000, 1:8000, etc.), from about 1:1 to about 1:1,000,or from about 1:1 to about 1:100. These molar ratios reflect the ratioof ansa-metallocene compound to the total amount of organoaluminumcompound in both the precontacted mixture and the postcontacted mixture,combined.

When a precontacting step is used, the molar ratio of olefin monomer toansa-metallocene compound in the precontacted mixture may be from about1:10 to about 100,000:1 (e.g., 1:10, 1:5, 1:1, 5:1, 5000:1, 10,000:1,50,000:1, etc.), or from about 10:1 to about 1,000:1. The weight ratioof the solid oxide activator to the organoaluminum compound may rangefrom about 1:5 to about 1,000:1, from about 1:3 to about 100:1, or fromabout 1:1 to about 50:1. The weight ratio of the ansa-metallocene tosolid oxide activator-support may be from about 1:1 to about 1:1,000,000(e.g., 1:2, 1:10, 1:5,000, 1:100,000, etc.), from about 1:10 to about1:100,000, or from about 1:20 to about 1:1000.

D. Examples of a Process to Prepare a Catalyst Composition

Embodiments of the present techniques may include processes to produce acatalyst composition. For example, one such process may includecontacting an ansa-metallocene, an olefin, and an organoaluminumcompound for a first period of time to form a precontacted mixtureincluding a precontacted ansa-metallocene, a precontacted organoaluminumcompound, and a precontacted olefin. The precontacted mixture may thenbe contacted with an activator-support and optionally additionalorganoaluminum compound for a second period of time to form apostcontacted mixture including a postcontacted ansa-metallocene, apostcontacted organoaluminum compound, a postcontacted olefin, and apostcontacted activator-support. In embodiments, the ansa-metallocenemay include a compound having the formula:(X¹)(X²)(X³)(X⁴)M¹;in which M¹ may be titanium, zirconium, or hafnium. X¹ may be asubstituted cyclopentadienyl, a substituted indenyl, or a substitutedfluorenyl. X² may be a substituted cyclopentadienyl or a substitutedfluorenyl.

One substituent on X¹ and X² is a bridging group having the formulaE(Cyc), wherein E may be a carbon atom, a silicon atom, a germaniumatom, or a tin atom, and E is bonded to both X¹ and X², and wherein Cycmay be a substituted or an unsubstituted carbon chain of from 4 to 6carbon atoms in length with each end connected to E to form a ringstructure. One substituent on X² may be a substituted or anunsubstituted alkyl or alkenyl group having up to 12 carbon atoms.

X³ and X⁴ may be independently: F, Cl, Br, or I; a hydrocarbyl grouphaving up to 20 carbon atoms, H, or BH₄; a hydrocarbyloxide group, ahydrocarbylamino group, or a trihydrocarbylsilyl group, any of whichhaving up to 20 carbon atoms; or OBR^(A) ₂ or SO₃R^(A), wherein R^(A)may be an alkyl group or an aryl group, any of which having up to 12carbon atoms.

Any additional substituent on the substituted cyclopentadienyl,substituted indenyl, substituted fluorenyl, or substituted alkyl groupmay be independently an aliphatic group, an aromatic group, a cyclicgroup, a combination of aliphatic and cyclic groups, an oxygen group, asulfur group, a nitrogen group, a phosphorus group, an arsenic group, acarbon group, a silicon group, or a boron group, any of which havingfrom 1 to 20 carbon atoms; a halide; or hydrogen.

E. Activity of the Catalyst Composition

The catalytic activity of the catalyst of the present techniques may begreater than or equal to about 1000 grams polyethylene per gram ofchemically treated solid oxide per hour (abbreviated gP/(g CTSO·hr)),greater than or equal to about 3000 gP/(g CTSO·hr), greater than orequal to about 6000 gP/(g CTSO·hr), or greater than or equal to about9000 gP/(g CTSO·hr). Activity may be measured under slurrypolymerization conditions using isobutane as the diluent, with apolymerization temperature from about 80° C. to about 100° C., and anethylene pressure of about 340 psig to about 550 psig. The reactorshould have substantially no indication of any wall scale, coating orother forms of fouling when making these measurements.

III. Use of the Catalyst Composition in Polymerization Processes

The catalysts of the present techniques are intended for any olefinpolymerization method, using various types of polymerization reactors.As used herein, “polymerization reactor” includes any polymerizationreactor capable of polymerizing olefin monomers to produce homopolymersor copolymers. Such homopolymers and copolymers may be referred to asresins or polymers. The various types of reactors include those that maybe referred to as batch, slurry, gas-phase, solution, high pressure,tubular or autoclave reactors. Gas phase reactors may include fluidizedbed reactors or staged horizontal reactors. Slurry reactors may includevertical or horizontal loops. High pressure reactors may includeautoclave or tubular reactors. Reactor types may include batch orcontinuous processes. Continuous processes could use intermittent orcontinuous product discharge. Processes may also include partial or fulldirect recycle of un-reacted monomer, un-reacted comonomer, and/ordiluent.

Polymerization reactor systems of the present techniques may include onetype of reactor in a system or multiple reactors of the same ordifferent type. Production of polymers in multiple reactors may includeseveral stages in at least two separate polymerization reactorsinterconnected by a transfer device making it possible to transfer thepolymers resulting from the first polymerization reactor into the secondreactor. The desired polymerization conditions in one of the reactorsmay be different from the operating conditions of the other reactors.Alternatively, polymerization in multiple reactors may include themanual transfer of polymer from one reactor to subsequent reactors forcontinued polymerization. Multiple reactor systems may include anycombination including, but not limited to, multiple loop reactors,multiple gas reactors, a combination of loop and gas reactors, multiplehigh pressure reactors or a combination of high pressure with loopand/or gas reactors. The multiple reactors may be operated in series orin parallel.

A. Loop Slurry Polymerization Processes

In embodiments of the present techniques, the polymerization reactorsystem may include a loop slurry reactor. Such reactors may includevertical or horizontal loops. Monomer, diluent, catalyst and optionallyany comonomer may be continuously fed to the loop reactor wherepolymerization occurs. Generally, continuous processes may include thecontinuous introduction of a monomer, a catalyst, and a diluent into apolymerization reactor and the continuous removal from this reactor of asuspension including polymer particles and the diluent. Reactor effluentmay be flashed to remove the solid polymer from the liquids that includethe diluent, monomer and/or comonomer. Various technologies may beemployed for this separation step including but not limited to: flashingthat may include any combination of heat addition and pressurereduction; separation by cyclonic action in either a cyclone orhydrocyclone; or separation by centrifugation.

Loop slurry polymerization processes (also known as the particle formprocess) are disclosed, for example, in U.S. Pat. Nos. 3,248,179,4,501,885, 5,565,175, 5,575,979, 6,239,235, 6,262,191 and 6,833,415,each of which is incorporated by reference in its entirety herein.

Diluents that may be used in slurry polymerization for example, themonomer being polymerized and hydrocarbons that are liquids underreaction conditions. Examples of such diluents may include, for example,hydrocarbons such as propane, cyclohexane, isobutane, n-butane,n-pentane, isopentane, neopentane, and n-hexane. Some looppolymerization reactions can occur under bulk conditions where nodiluent may be used or where the monomer (e.g., propylene) acts as thediluent. An example is polymerization of propylene monomer as disclosedin U.S. Pat. No. 5,455,314, which is incorporated by reference herein inits entirety.

B. Gas Phase Polymerization Processes

Further, the polymerization reactor may include a gas phase reactor.Such systems may employ a continuous recycle stream containing one ormore monomers continuously cycled through a fluidized bed in thepresence of the catalyst under polymerization conditions. A recyclestream may be withdrawn from the fluidized bed and recycled back intothe reactor. Simultaneously, polymer product may be withdrawn from thereactor and new or fresh monomer may be added to replace the polymerizedmonomer. Such gas phase reactors may include a process for multi-stepgas-phase polymerization of olefins, in which olefins are polymerized inthe gaseous phase in at least two independent gas-phase polymerizationzones while feeding a catalyst-containing polymer formed in a firstpolymerization zone to a second polymerization zone. One type of gasphase reactor is disclosed in U.S. Pat. Nos. 5,352,749, 4,588,790 and5,436,304, each of which is incorporated by reference in its entiretyherein.

According to still another aspect of the techniques, a high pressurepolymerization reactor may include a tubular reactor or an autoclavereactor. Tubular reactors may have several zones where fresh monomer,initiators, or catalysts are added. Monomer may be entrained in an inertgaseous stream and introduced at one zone of the reactor. Initiators,catalysts, and/or catalyst components may be entrained in a gaseousstream and introduced at another zone of the reactor. The gas streamsmay be intermixed for polymerization. Heat and pressure may be employedappropriately to obtain optimal polymerization reaction conditions.

C. Solution Polymerization Processes

According to yet another aspect of the techniques, the polymerizationreactor may include a solution polymerization reactor wherein themonomer may be contacted with the catalyst composition by suitablestifling or other means. A carrier including an inert organic diluent orexcess monomer may be employed. If desired, the monomer may be broughtin the vapor phase into contact with the catalytic reaction product, inthe presence or absence of liquid material. The polymerization zone maybe maintained at temperatures and pressures that will result in theformation of a solution of the polymer in a reaction medium. Agitationmay be employed to obtain better temperature control and to maintainuniform polymerization mixtures throughout the polymerization zone.Adequate means may be utilized for dissipating the exothermic heat ofpolymerization.

D. Reactor Support Systems

Polymerization reactors suitable for the present techniques may furtherinclude any combination of a raw material feed system, a feed system forcatalyst or catalyst components, and/or a polymer recovery system.Suitable reactor systems for the present techniques may further includesystems for feedstock purification, catalyst storage and preparation,extrusion, reactor cooling, polymer recovery, fractionation, recycle,storage, loadout, laboratory analysis, and process control.

E. Polymerization Conditions

Conditions that may be controlled for polymerization efficiency and toprovide resin properties include temperature, pressure and theconcentrations of various reactants. Polymerization temperature canaffect catalyst productivity, polymer molecular weight and molecularweight distribution. Suitable polymerization temperature may be anytemperature below the de-polymerization temperature according to theGibbs Free energy equation. Typically this includes from about 60° C. toabout 280° C., for example, or from about 70° C. to about 110° C.,depending upon the type of polymerization reactor.

Suitable pressures will also vary according to the reactor andpolymerization type. The pressure for liquid phase polymerizations in aloop reactor is typically less than 1000 psig. Pressure for gas phasepolymerization is usually at about 200-500 psig. High pressurepolymerization in tubular or autoclave reactors is generally run atabout 20,000 to 75,000 psig. Polymerization reactors may also beoperated in a supercritical region occurring at generally highertemperatures and pressures. Operation above the critical point of apressure/temperature diagram (supercritical phase) may offer advantages.

The concentration of various reactants may be controlled to produceresins with certain physical and mechanical properties. The proposedend-use product that will be formed by the resin and the method offorming that product determines the desired resin properties. Mechanicalproperties include tensile, flexural, impact, creep, stress relaxationand hardness tests. Physical properties include density, molecularweight, molecular weight distribution, melting temperature, glasstransition temperature, temperature melt of crystallization, density,stereoregularity, crack growth, long chain branching and rheologicalmeasurements.

The concentrations of monomer, co-monomer, hydrogen, co-catalyst,modifiers, and electron donors may be important in producing these resinproperties. Comonomer may be used to control product density. Hydrogenmay be used to control product molecular weight. Co-catalysts may beused to alkylate, scavenge poisons and control molecular weight.Modifiers may be used to control product properties and electron donorsaffect stereoregularity. In addition, the concentration of poisons mustbe minimized since they impact the reactions and product properties.

F. Final Products Made from Polymers

The polymer or resin fluff from the reactor system may have additivesand modifiers added to provide better processing during manufacturingand for desired properties in the end product. Additives include surfacemodifiers such as slip agents, antiblocks, tackifiers; antioxidants suchas primary and secondary antioxidants; pigments; processing aids such aswaxes/oils and fluoroelastomers; and special additives such as fireretardants, antistats, scavengers, absorbers, odor enhancers, anddegradation agents. After the addition of the additives, the polymer orresin fluff may be extruded and formed into pellets for distribution tocustomers and formation into final end-products.

To form end-products or components from the pellets, the pellets aregenerally subjected to further processing, such as blow molding,injection molding, rotational molding, blown film, cast film, extrusion(e.g., sheet extrusion, pipe and corrugated extrusion,coating/lamination extrusion, etc.), and so on. Blow molding is aprocess used for producing hollow plastic parts. The process typicallyemploys blow molding equipment, such as reciprocating screw machines,accumulator head machines, and so on. The blow molding process may betailored to meet the customer's needs, and to manufacture productsranging from the plastic milk bottles to the automotive fuel tanksmentioned above. Similarly, in injection molding, products andcomponents may be molded for a wide range of applications, includingcontainers, food and chemical packaging, toys, automotive, crates, capsand closures, to name a few.

Profile extrusion processes may also be used. Polyethylene pipe, forexample, may be extruded from polyethylene pellet resins and used in anassortment of applications due to its chemical resistance, relative easeof installation, durability and cost advantages, and the like. Indeed,plastic polyethylene piping has achieved significant use for watermains, gas distribution, storm and sanitary sewers, interior plumbing,electrical conduits, power and communications ducts, chilled waterpiping, well casing, to name a few applications. In particular,high-density polyethylene (HDPE), which generally constitutes thelargest volume of the polyolefin group of plastics used for pipe, may betough, abrasion-resistant and flexible (even at subfreezingtemperatures). Furthermore, HDPE pipe may be used in small diametertubing and in pipe up to more than 8 feet in diameter. In general,polyethylene pellets (resins) may be supplied for the pressure pipingmarkets, such as in natural gas distribution, and for the non-pressurepiping markets, such as for conduit and corrugated piping.

Rotational molding is a high-temperature, low-pressure process used toform hollow parts through the application of heat to biaxially-rotatedmolds. Polyethylene pellet resins generally applicable in this processare those resins that flow together in the absence of pressure whenmelted to form a bubble-free part. Resins, such as those produced by thecatalyst compositions of the present techniques, may offer such flowcharacteristics, as well as a wide processing window. Furthermore, thesepolyethylene resins suitable for rotational molding may exhibitdesirable low-temperature impact strength, good load-bearing properties,and good ultraviolet (UV) stability. Accordingly, applications forrotationally-molded polyolefin resins include agricultural tanks,industrial chemical tanks, potable water storage tanks, industrial wastecontainers, recreational equipment, marine products, plus many more.

Sheet extrusion is a technique for making flat plastic sheets from avariety of resins. The relatively thin gauge sheets are generallythermoformed into packaging applications such as drink cups, delicontainers, produce trays, baby wipe containers and margarine tubs.Other markets for sheet extrusion of polyolefin include those thatutilize relatively thicker sheets for industrial and recreationalapplications, such as truck bed liners, pallets, automotive dunnage,playground equipment, and boats. A third use for extruded sheet, forexample, is in geomembranes, where flat-sheet polyethylene material maybe welded into large containment systems for mining applications andmunicipal waste disposal.

The blown film process is a relatively diverse conversion system usedfor polyethylene. The American Society for Testing and Materials (ASTM)defines films as less than 0.254 millimeter (10 mils) in thickness.However, the blown film process can produce materials as thick as 0.5millimeter (20 mils), and higher. Furthermore, blow molding inconjunction with monolayer and/or multilayer coextrusion technologieslay the groundwork for several applications. Advantageous properties ofthe blow molding products may include clarity, strength, tearability,optical properties, and toughness, to name a few. Applications mayinclude food and retail packaging, industrial packaging, andnon-packaging applications, such as agricultural films, hygiene film,and so forth.

The cast film process may differ from the blown film process through thefast quench and virtual unidirectional orientation capabilities. Thesecharacteristics allow a cast film line, for example, to operate athigher production rates while producing beneficial optics. Applicationsin food and retail packaging take advantage of these strengths. Finally,polyolefin pellets may also be supplied for the extrusion coating andlamination industry.

Ultimately, the products and components formed from polyolefin (e.g.,polyethylene) pellets may be further processed and assembled fordistribution and sale to the consumer. For example, a polyethylene milkbottle may be filled with milk for distribution to the consumer, or thefuel tank may be assembled into an automobile for distribution and saleto the consumer.

IV. Examples of Polymers Prepared Using the Catalysts of the PresentTechniques

Without intending to be limiting, ethylene polymers produced usingcatalyst compositions of the present techniques may be characterized byhigher comonomer incorporation than may be observed when usingtightly-bridged ansa-metallocene catalysts without a cyclic bridgingmoiety connecting the two η⁵-cyclopentadienyl-type ligands. This may bedemonstrated by the polymerization runs shown in Table 1.

TABLE 1 Exemplary Polymerization Runs Activity Metallocene 1- 1-Hexene1-Hexene (g P/g Run (mmol × Time Hexene Solid PE Activity (butyl)(butyl) CTSO/ No.* Metallocene 10{circumflex over ( )}3) (min) (g) (g)(g/mmol/hr) (mol %) (wt %) hr) 1 I-1 0.94 30 10.0 130.0 4255 0.69 2.032600 2 I-2 0.95 45 10.0 128.0 2807 0.66 1.97 1707 3 C-1 0.94 240 10.0116.0 532 0.37 1.11 290 4 C-2 0.94 37 10.0 132.0 3450 0.64 1.89 2141 5C-3 0.95 47 10.0 121.0 2688 0.56 1.66 1545 6 I-1 0.94 21 20.0 125.0 60792.05 5.90 3571 7 I-2 0.95 25 20.0 116.0 5053 1.92 5.54 2784 8 C-1 0.94250 20.0 98.0 511 0.91 2.68 235 9 C-2 0.94 32 20.0 137.0 3989 1.43 4.172569 10 C-3 0.95 47 20.0 139.0 2688 1.26 3.69 1774 11 I-1 0.94 19 30.0128.0 6719 3.28 9.23 4042 12 I-2 0.95 22 30.0 124.0 5742 3.02 8.53 338213 C-1 0.94 130 30.0 118.0 982 2.33 6.69 545 14 C-2 0.94 19 30.0 124.06719 2.42 6.94 3916 15 C-3 0.95 30 30.0 121.0 4211 1.96 5.67 2420 *Allpolymerizations were conducted using: 80° C.; maintaining a 340 psipressure of ethylene in the reactor; 100 mg sulfated alumina; and 0.5mmol TnBA.

Runs 1, 2, 6, 7, 11, and 12 in Table 1 show results that may be obtainedfor polymers made using exemplary catalysts in accordance with thepresent techniques. The specific metallocene structures used, I-1 andI-2, are shown in FIG. 1, which correspond to the identification givenin the column labeled “Metallocene,” in Table 1. In comparison, Runs3-5, 8-10, and 13-15 in Table 1 show comparative results that may beobtained for polymers made from a catalysts that do not have a cyclicbridging moiety connecting the η⁵-cyclopentadienyl-type ligands. Themetallocene structure used for these runs is shown in FIG. 2 asstructures C-1, C-2, and C-3.

Comonomer Incorporation

The catalyst compositions of the present techniques may have bettercomonomer incorporation than ansa-metallocene catalyst systems that donot have a cyclic bridging moiety connecting the two115-cyclopentadienyl-type ligands. This may be shown by the comparisonof Runs 1 and 2, in Table 1, with Runs 3, 4, and 5.

In Runs 1-5, 10 grams of 1-hexene were added to the reactor as acomonomer. The amounts of comonomer incorporated into the final polymerare shown as mol % and wt % of 1-hexene in Table 1. In all cases, theamount of 1-hexene incorporated into polymers made using the exemplarycatalysts, shown in Runs 1 and 2, was higher than for comparativeansa-metallocenes, shown in Runs 3-5.

Further comparisons are shown in Runs 6-10. In these runs, 20 grams of1-hexene comonomer were added to the reactor. As shown by Runs 6 and 7,comonomer incorporation for the exemplary catalysts of the presenttechniques was also improved over the comparative metallocenes shown inRuns 8-10.

Another comparison is shown by Runs 11-15. In these runs, 30 grams of1-hexene comonomer were added to the reactor. Again, the exemplarypolymers of the current techniques showed higher comonomer incorporationthan the comparative metallocenes listed in Runs 13-15. Thus, at allevels of co-monomer tested, exemplary catalyst compositions of thepresent techniques were more effective at incorporating comonomer.

V. Procedures

A. Pore Size Determination

A Quantachrome Autosorb-6 Nitrogen Pore Size Distribution Instrument wasused to determine specific surface area (“surface area”) and specificpore volume (“pore volume”). This instrument was acquired from theQuantachrome Corporation, Syosset, N.Y.

B. Measurement of Comonomer Incorporation by C-13 NMR

Hexene incorporation was obtained from measuring butyl branch content inthe copolymers on a Varian Inova-500 spectrometer using classical ¹³CNMR spectroscopy techniques as previously described [see Randall, J. C.,Hsieh, E. T., NMR and Macromolecules; Sequence, Dynamic, and DomainStructure, ACS Symposium Series 247, J. C. Randall, Ed., AmericanChemical Society, Washington D.C., 1984]. The samples were prepared at135° C. at 10 wt % in a 1:6 mixture of 1,4-dichlorobenzene-d₄ (DCB-d₄)and 1,2,4-trichlorobenzene (TCB). The spectra were acquired at 125° C.using a 90° pulse width, a 10 second pulse delay and full nuclearOverhauser effect. Decoupling was accomplished using a Waltz-16 pulsesequence.

C. Preparation of a Fluorided Silica-Alumina Activator-Support

The silica-alumina used to prepare the fluorided silica-alumina acidicactivator-support in this Example was typically Davison silica-aluminaobtained from W.R. Grace as Grade MS 13-110, containing 13% alumina,having a pore volume of about 1.2 cc/g and a surface area of about 400m²/g. This material was fluorided by impregnation to incipient wetnesswith a solution containing ammonium bifluoride in an amount sufficientto equal 10 wt % of the weight of the silica-alumina. This impregnatedmaterial was then dried in a vacuum oven for 8 hours at 100° C. Thethus-fluorided silica-alumina samples were then calcined. Calcinationwas performed by placing about 10 grams of the alumina in a 1.75-inchquartz tube fitted with a sintered quartz disk at the bottom. While thesilica was supported on the disk, dry air was blown up through the diskat the linear rate of about 1.6 to 1.8 standard cubic feet per hour. Anelectric furnace around the quartz tube was employed to increase thetemperature of the tube at the rate of about 400° C. per hour to a finaltemperature of about 500° C. At this temperature, the silica-alumina wasallowed to fluidize for about three hours in the dry air. Afterward, thesilica-alumina was collected and stored under dry nitrogen, and was usedwithout exposure to the atmosphere.

D. Preparation of a Sulfated Alumina Activator-Support

Sulfated alumina was formed by a process wherein alumina waschemically-treated with a sulfate or bisulfate source. Such a sulfate orbisulfate source may include, for example, sulfuric acid, ammoniumsulfate, or ammonium bisulfate.

In an exemplary procedure, a commercial alumina sold as W.R. GraceAlumina A was sulfated by impregnation with an aqueous solutioncontaining about 15-20% (NH₄)₂SO₄ or H₂SO₄. This sulfated alumina wascalcined at 550° C. in air (240° C./h ramp rate), with a 3 h hold periodat this temperature. Afterward, the alumina was collected and storedunder dry nitrogen, and was used without exposure to the atmosphere.

E. Preparation Procedures for Exemplary Metallocenes and Polymers

Compounds F-3, L-3, and C-1 (shown in FIG. 2) were prepared using theprocedure disclosed in U.S. Pat. No. 7,064,225, herein included byreference in its entirety. Preparation procedures for the other fulveneswhose chemical structures are shown below, are presented in thefollowing subsections: 1 (F-1), 2 (F-2), 3 (F-4), and 4 (F-5).

After preparation, these fulvenes were used to prepare the ligands whosechemical structures are listed below, as presented in the followingsubsections: 5 (L-1), 6 (L-2), 7 (L-4), and 8 (L-5).

Procedures using ligands L-1, L-2, L-4, and L-5 to prepare the exemplarymetallocenes are presented in subsections 9 (I-1) and 10 (I-2), andprocedures for preparing comparative metallocenes are presented insubsections 11 (C-2) and 12 (C-3). Subsection 13 presents exemplaryprocedures for preparing polymers using the catalyst compositions of thepresent techniques.

Unless specified otherwise, reagents were obtained from Aldrich ChemicalCompany and were used as received. 2,7-Di-tert-butylfluorene waspurchased from Degussa. The Grignard reagent CpMgCl (1M in THF) waspurchased from Boulder Scientific Company. Zirconium(IV) chloride waspurchased from Strem. The solvent tetrahydrofuran THF was distilled frompotassium, while anhydrous diethyl ether, dichloromethane, n-pentane,and toluene were purchased from Fisher Scientific Company and storedover activated alumina. All solvents were degassed and stored undernitrogen. Reported preparations were not optimized.

1. Synthesis of 2-(buten-3-yl)-6,6-pentamethylenepentafulvene (F-1)

To 2-(buten-3-yl)cyclopentadiene (0.127 mol) dissolved in methanol (50mL) was added cyclohexanone (12 g) followed by pyrrolidine (17 mL) at 0°C. The mixture was kept at 0° C. for an additional 30 minutes, thenwarmed up to room temperature and stirred overnight. The reaction wasquenched with a mixture of ice and acetic acid. The mixture wasextracted with pentane. The organic layer was washed with water anddried over anhydrous sodium sulfate. Removal of the solvent under vacuumgave a brown oil. The crude product was purified through silica columnwith heptane. The desired product (13 g, 54% yield) was obtained as ayellow liquid.

2. Synthesis of 2-(buten-3-yl)-6,6-tetramethylenepentafulvene (F-2)

To 2-(buten-3-yl)cyclopentadiene (75 mmol) dissolved in methanol (25 mL)was added cyclopentanone (7.6 g) followed by pyrrolidine (12.8 mL) at 0°C. The mixture was kept at 0° C. for an additional 5 minutes, thenwarmed up to room temperature and stirred overnight. The reaction wasquenched with a mixture of ice and acetic acid. The mixture wasextracted with pentane. The organic layer was washed with water anddried over anhydrous sodium sulfate. Removal of the solvent under vacuumgave a brown oil. The crude product was purified through silica columnwith heptane. The desired product (7.9 g, 56.6% yield) was obtained as ayellow liquid.

3. Synthesis of 2-(buten-3-yl)-6,6-diphenylpentafulvene (F-4)

To 4-bromo-1-butene (100 g of 97 wt %, 0.719 mol) was addedcyclopentadienyl magnesium chloride (800 mL of 1 M solution in THF, 0.8mol) at 0° C. in 50 minutes. After stifling for an additional 15 minutesat 0° C., the mixture was warmed to room temperature. After stirringovernight, the reaction was quenched with a mixture of ice and water.The mixture was extracted with pentane. The organic layer was washedwith water and dried over anhydrous sodium sulfate. Removal of thesolvent under vacuum at room temperature gave a brown liquid (94.2 g,crude buten-3-ylcyclopentadiene). To the crude buten-3-ylcyclopentadiene(94.2 g) dissolved in THF (500 mL) was added n-BuLi (70 mL of 10 M inhexanes, 0.7 mol) at −78° C. The mixture was warmed up to roomtemperature and stirred overnight. The anion solution was added tobenzophenone (133.8 g, 0.735 mol) dissolved in THF (400 mL) at 0° C. in35 minutes. The mixture was warmed to room temperature and stirredovernight. The reaction was quenched with a mixture of ice and 10% HClaqueous solution. The mixture was extracted with pentane. The organiclayer was washed with water and dried over anhydrous sodium sulfate.Removal of the solvent under vacuum at 40° C. gave a dark red viscousoil. The oil was dissolved in heptane and filtered through silica gel.The product was collected by washing the silica gel with 5-10% CH₂Cl₂ inheptane. Removal of the solvent gave the desired product (152 g, 74.4%yield based on 4-bromo-1-butene) as a dark red viscous oil.

4. Synthesis of 2-(penten-4-yl)-6,6-diphenylpentafulvene (F-5)

To 5-bromo-1-pentene (100 g of 95 wt %, 0.637 mol) was addedcyclopentadienyl magnesium chloride (700 mL of 1 M solution in THF, 0.7mol) at 0° C. in an hour. After stirring for an additional 30 minutes at0° C., the mixture was warmed to room temperature. After stiflingovernight, the reaction was quenched with a mixture of ice and water.The mixture was extracted with pentane. The organic layer was washedwith water and dried over anhydrous sodium sulfate. Removal of thesolvent under vacuum at room temperature gave a yellow-brown liquid (98g, crude penten-4-ylcyclopentadiene). To the crudepenten-4-yl-cyclopentadiene (89 g, ca. 0.579 mol, theoretical number=(89/98)*0.637) dissolved in THF (500 mL) was added n-BuLi (60 mL of 10 Min hexanes, 0.6 mol) at −78° C. The mixture was warmed up to roomtemperature and stirred overnight. The anion solution was added tobenzophenone (110 g, 0.604 mol) dissolved in THF (500 mL) at 0° C. in 25minutes. The mixture was warmed to room temperature and stirredovernight. The reaction was quenched with a mixture of ice and 10% HClaqueous solution. The mixture was extracted with pentane. The organiclayer was washed with water and dried over anhydrous sodium sulfate.Removal of the solvent under vacuum at 40° C. gave a dark red viscousoil. The oil was dissolved in heptane and filtered through silica gel.The product was collected by washing the silica gel with 5-10% CH₂Cl₂ inheptane. Removal of the solvent gave the desired product (145 g, 84%yield based on 5-bromo-1-pentene) as a dark red viscous oil.

5. Synthesis of1-(3-(buten-3-yl)cyclopentadien-1-yl)-1-(2,7-di-tert-butylfluoren-9-yl)cyclohexane(L-1)

To 2,7-di-tert-butylfluorene (18 g, 65 mmol) dissolved in Et₂O (100 mL)was added n-BuLi (6.8 mL of 10 M in hexanes, 68 mmol) at 0° C. Themixture was warmed to room temperature and stirred overnight. The anionsolution was added to 2-(buten-3-yl)-6,6-pentamethylenepentafulvene(F-1) (13 g, 65 mmol) dissolved in Et₂O (100 mL) at −78° C. in 5minutes. The mixture was warmed to room temperature and stirred for fourdays. The reaction was quenched with a mixture of saturated NH₄Claqueous solution. The mixture was extracted with Et₂O. The organic layerwas washed with water and dried over anhydrous sodium sulfate. Removalof the solvent under vacuum gave a red-brown oil. The crude product waspurified through silica column with 5-10% CH₂Cl₂ in heptane. A mixtureof isomers for the desired product (24.1 g, 77.6% yield) was obtained asa viscous oil.

6. Synthesis of1-(3-(buten-3-yl)cyclopentadien-1-yl)-1-(2,7-di-tert-butylfluoren-9-yl)cyclopentane(L-2)

To 2,7-di-tert-butylfluorene (11.8 g, 42.4 mmol) dissolved in Et₂O (100mL) was added n-BuLi (4.5 mL of 10 M in hexanes, 45 mmol) at 0° C. Themixture was warmed to room temperature and stirred overnight. The anionsolution was added to 2-(buten-3-yl)-6,6-tetramethylenepentafulvene(F-2) (7.9 g, 42.4 mmol) dissolved in Et₂O (20 mL) at −78° C. Themixture was warmed to room temperature and stirred overnight. Thereaction was quenched with a mixture of saturated NH₄Cl aqueoussolution. The mixture was extracted with Et₂O. The organic layer waswashed with water and dried over anhydrous sodium sulfate. Removal ofthe solvent under vacuum gave a viscous oil. The crude product waspurified through silica column with heptane. A mixture of isomers forthe desired product (5.4 g, 27.7% yield) was obtained as a viscous oil.

7. Synthesis of1-(3-(buten-3-yl)cyclopentadien-1-yl)-1-(2,7-di-tert-butylfluoren-9-yl)-1,1-diphenylmethane(L-4)

To 2,7-di-tert-butylfluorene (91.7 g, 0.33 mol) dissolved in Et₂O (500mL) was added n-BuLi (35 mL of 10 M in hexanes, 0.35 mol) at 0° C. Themixture was warmed to room temperature and stirred overnight. The anionsolution was added to 2-(buten-3-yl)-6,6-diphenylpentafulvene (104 g,0.366 mol) (F-4) dissolved in Et₂O (200 mL) at 0° C. in 35 minutes.After stirring for an additional 30 minutes at 0° C., the mixture waswarmed to room temperature and stirred overnight. The reaction wasquenched with a mixture of ice and 10% HCl aqueous solution. The mixturewas extracted with CH₂Cl₂. The organic layer was washed with water anddried over anhydrous sodium sulfate. Removal of the solvent under vacuumgave a pale brown solid. The solid was washed with heptane and driedunder vacuum. A mixture of isomers for the desired product (142 g, 76.5%yield) was obtained as a white solid.

8. Synthesis of1-(3-(penten-4-yl)cyclopentadien-1-yl)-1-(2,7-di-tert-butylfluoren-9-yl)-1,1-diphenylmethane(L-5)

To 2,7-di-tert-butylfluorene (125.1 g, 0.45 mol) dissolved in Et₂O (700mL) was added n-BuLi (47 mL of 10 M in hexanes, 0.47 mol) at 0° C. Themixture was warmed to room temperature and stirred overnight. The anionsolution was added to 2-(penten-4-yl)-6,6-diphenylpentafulvene (145 g,0.487 mol) (F-5) dissolved in Et₂O (300 mL) at −78° C. in 10 minutes.The mixture was warmed to room temperature and stirred overnight. Thereaction was quenched with a mixture of ice and 10% HCl aqueoussolution. The mixture was extracted with Et₂O. The organic layer waswashed with water and dried over anhydrous sodium sulfate. Removal ofthe solvent under vacuum gave a pale brown solid. The solid was washedwith heptane and dried under vacuum. A mixture of isomers for thedesired product (191.7 g, 74% yield) was obtained as a white solid.

9. Synthesis ofcyclohexylidene(η⁵-(3-(buten-3-yl)cyclopentadien-1-ylidene)(η⁵-2,7-di-tert-butylfluoren-9-ylidene)zirconiumdichloride (I-1 in FIG. 1)

To1-(3-(buten-3-yl)cyclopentadien-1-yl)-1-(2,7-di-tert-butylfluoren-9-yl)cyclohexane(L-1) (14.8 g, 31 mmol) dissolved in Et₂O (150 mL) was slowly addedn-BuLi (6.8 mL of 10 M in hexanes, 68 mmol) at 0° C. The mixture waswarmed to room temperature, stirred overnight, and then added viacannula to ZrCl₄ (8.2 g, 35 mmol) suspended in a mixture of pentane (140mL) and Et₂O (20 mL) at 0° C. in 10 minutes. The mixture was warmed toroom temperature, stirred overnight, and evacuated to dryness. Theresidue was stirred in pentane (150 mL) and centrifuged. The supernatantwas discarded. The remaining solid was washed a second time with pentane(50 mL), then extracted with methylene chloride and centrifuged. Thesolution was taken to dryness under vacuum to give an orange-red solid(7.8 g, 39.4% yield).

10. Synthesis ofcyclopentylidene(η⁵-(3-(buten-3-yl)cyclopentadien-1-ylidene)(η⁵-2,7-di-tert-butylfluoren-9-ylidene)zirconiumdichloride (I-2 in FIG. 1)

To1-(3-(buten-3-yl)cyclopentadien-1-yl)-1-(2,7-di-tert-butylfluoren-9-yl)cyclopentane(L-2) (5.4 g, 11.6 mmol) dissolved in Et₂O (60 mL) was slowly addedn-BuLi (2.4 mL of 10 M in hexanes, 24 mmol) at 0° C. The mixture waswarmed to room temperature, stirred overnight, and then added viacannula to ZrCl₄ (3 g, 12.9 mmol) suspended in a mixture of pentane (60mL) and Et₂O (10 mL) at 0° C. The mixture was warmed to roomtemperature, stirred overnight, and evacuated to dryness. The residuewas stirred in pentane (50 mL) and centrifuged. The supernatant wasdiscarded. The remaining solid was washed a second time with pentane (50mL), then extracted with methylene chloride and centrifuged. Thesolution was taken to dryness under vacuum to give an orange-red solid(4.3 g, 59.4% yield).

11. Synthesis ofdiphenylmethylidene(η⁵-(3-(buten-3-yl)cyclopentadien-1-ylidene)(η⁵-2,7-di-tert-butylfluoren-9-ylidene)zirconiumdichloride (C-2 in FIG. 2)

To1-(3-(buten-3-yl)cyclopentadien-1-yl)-1-(2,7-di-tert-butylfluoren-9-yl)-1,1-diphenylmethane(40.5 g, 72.1 mmol) (L-4) suspended in Et₂O (400 mL) was slowly addedn-BuLi (15.2 mL of 10 M in hexanes, 152 mmol) at 0° C. The mixture waswarmed to room temperature, stirred overnight, and then added viacannula to ZrCl₄ (18.5 g, 79.4 mmol) suspended in a mixture of pentane(400 mL) and Et₂O (30 mL) at 0° C. in 15 minutes. The mixture was warmedto room temperature, stirred for one day, and evacuated to dryness. Theresidue was stirred in pentane (300 mL) and centrifuged. The supernatantwas discarded. The remaining solid was washed a second time with pentane(100 mL), then extracted with methylene chloride and centrifuged. Thesolution was taken to dryness under vacuum to give an orange-red solid(38.1 g, 73.3% yield).

12. Synthesis ofdiphenylmethylidene(η⁵-(3-(penten-4-yl)cyclopentadien-1-ylidene)(η⁵-2,7-di-tert-butylfluoren-9-ylidene)zirconiumdichloride (C-3 in FIG. 2)

To1-(3-(penten-4-yl)cyclopentadien-1-yl)-1-(2,7-di-tert-butylfluoren-9-yl)-1,1-diphenylmethane(34.7 g, 60.2 mmol) (L-5) dissolved in Et₂O (300 mL) was slowly addedn-BuLi (52 mL of 2.5 M in hexanes, 130 mmol) at 0° C. The mixture waswarmed to room temperature, stirred overnight, and then added viacannula to ZrCl₄ (14.7 g, 63.1 mmol) suspended in a mixture of pentane(250 mL) and Et₂O (20 mL) at 0° C. in 30 minutes. The mixture was warmedto room temperature, stirred for one day, and evacuated to dryness. Theresidue was stirred in pentane (200 mL) and centrifuged. The supernatantwas discarded. The remaining solid was washed a second time with pentane(50 mL), then extracted with methylene chloride and centrifuged. Thesolution was taken to dryness under vacuum to give an orange-red solid(33.5 g, 75.6%).

13. Polymerization Procedures for Examples 1-15

Examples 1-15 in Table 1 illustrate ethylene polymerization runsperformed in a one-gallon (3.785 liter) stainless steel autoclavereactor at various temperatures, using two liters of isobutane diluentand an aluminum alkyl cocatalyst and scavenger. No hydrogen was added.Metallocene solutions (2 mg/mL) were typically prepared by dissolving 30mg of the metallocene in 15 mL of toluene. A typical polymerizationprocedure is as follows. The aluminum alkyl compound, treated solidoxide, and the metallocene solution were added through a charge port,typically in that order, while venting isobutane vapor. The appropriateamount of comonomer, as shown in Table 1, was added. The charge port wasclosed and two liters of isobutane were added. The contents of thereactor were stirred and heated to the desired run temperature. Ethylenewas fed on demand to maintain the specified pressure for the specifiedlength of the polymerization run. The reactor was maintained at thedesired run temperature through the run by an automated heating andcooling system.

After the allotted polymerization time, the ethylene flow was stopped,and the reactor slowly depressurized and opened to recover a granularpolymer. In all cases, the reactor was clean with no indication of anywall scale, coating or other forms of fouling. The polymer was thenremoved and weighed, giving the results listed in Tables 1, above.

While the invention may be susceptible to various modifications andalternative forms, specific embodiments have been shown by way ofexample in the drawings and are described in detail herein. However, itshould be understood that the invention is not intended to be limited tothe particular forms presented. Rather, the invention is to cover allmodifications, equivalents and alternatives falling within the spiritand scope of the invention as defined by the following appended claims.

1. An ansa-metallocene, comprising: a compound having the formula:(X¹)(X²)(X³)(X⁴)M¹, wherein: M¹ comprises titanium, zirconium, orhafnium; X¹ and X² independently comprise a substitutedcyclopentadienyl, a substituted indenyl, or a substituted fluorenyl; afirst substituent on X¹ and X² comprises a bridging group having theformula E(Cyc), wherein E is a carbon atom, a silicon atom, a germaniumatom, or a tin atom, and E is bonded to both X¹ and X², and wherein Cycis a substituted or an unsubstituted carbon chain of from 4 to 6 carbonatoms in length with each end of the substituted or unsubstituted carbonchain connected to E to form a ring structure; a second substituent onX¹ or X² comprises a substituted or an unsubstituted alkenyl group; andX³ and X⁴ independently comprise a halide, a hydrocarbyl group, H, BH₄,a hydrocarbyloxide group, a hydrocarbylamino group, atrihydrocarbylsilyl group, an amido group, a phosphido group, OBR^(A) ₂,or SO₃R^(A), wherein R^(A) is an alkyl group or an aryl group.
 2. Theansa-metallocene of claim 1, wherein an additional substituent on X¹ orX² comprises an aliphatic group, an aromatic group, a cyclic group, acombination of aliphatic and cyclic groups, an oxygen group, a sulfurgroup, a nitrogen group, a phosphorus group, an arsenic group, a carbongroup, a silicon group, or a boron group, or any combination thereof,and the additional substituent comprises between 1 and 20 carbons. 3.The ansa-metallocene of claim 1, wherein an additional substituent on X¹or X² comprises F, Cl, Br, I, or H.
 4. The ansa-metallocene of claim 1,wherein the second substituent comprises up to 20 carbons.
 5. Theansa-metallocene of claim 1, wherein the second substituent on X¹ or X²comprises up to 12 carbons.
 6. The ansa-metallocene of claim 1, whereinX¹ comprises substituted cyclopentadienyl and X² comprises substitutedfluorenyl.
 7. The ansa-metallocene of claim 1, wherein the secondsubstituent on X¹ or X² is a substituted alkenyl group substituted withan aliphatic group, an aromatic group, a cyclic group, a combination ofaliphatic and cyclic groups, an oxygen group, a sulfur group, a nitrogengroup, a phosphorus group, an arsenic group, a carbon group, a silicongroup, or a boron group, or any combination thereof.
 8. Theansa-metallocene of claim 1, wherein X³ and X⁴ independently comprise ahydrocarbyloxide group comprising up to 20 carbons or a hydrocarbylaminogroup comprising up to 20 carbons, OBR^(A) ₂, or SO₃R^(A), wherein R^(A)is an alkyl group or an aryl group having up to 12 carbons.
 9. Theansa-metallocene of claim 1, wherein Cyc is a substituted carbon chainsubstituted with an aliphatic group, an aromatic group, a cyclic group,a combination of aliphatic and cyclic groups, an oxygen group, a sulfurgroup, a nitrogen group, a phosphorus group, an arsenic group, a carbongroup, a silicon group, or a boron group.
 10. The ansa-metallocene ofclaim 1, wherein E(Cyc) has the formula C(CH₂CH₂CH₂CH₂),C(CH₂CH₂CH₂CH₂CH₂), Si(CH₂CH₂CH₂CH₂), Si(CH₂CH₂CH₂CH₂CH₂),Ge(CH₂CH₂CH₂CH₂), Ge(CH₂CH₂CH₂CH₂CH₂), Sn(CH₂CH₂CH₂CH₂), orSn(CH₂CH₂CH₂CH₂CH₂).
 11. An ansa-metallocene, comprising: a compoundhaving the formula:

wherein: M¹ is zirconium, hafnium, or titanium; X³ and X⁴ areindependently a halide, a hydrocarbyl, a trihydrocarbyl silyl, or aboron-containing group; E is C, Si, Ge, or Sn; n is an integer from 1 to3, inclusive; R^(3A) and R^(3B) are independently a hydrocarbyl group, atrihydrocarbylsilyl group, or hydrogen; m is an integer from 0 to 10,inclusive; and R^(4A) and R^(4B) are independently a hydrocarbyl groupor hydrogen.
 12. The ansa-metallocene of claim 11, wherein R^(3A) andR^(3B) independently comprise a hydrocarbyl group comprising up to 20carbon atoms or a trihydrocarbylsilyl group comprising up to 20 carbonatoms.
 13. The ansa-metallocene of claim 11, wherein R^(4A) and R^(4B)are independently a hydrocarbyl group group having up to 12 carbonatoms, or hydrogen.
 14. The ansa-metallocene of claim 11, wherein: M¹ iszirconium or hafnium; X³ and X⁴ are independently F, Cl, Br, or I; E isC or Si; R^(3A) and R^(3B) are independently H, methyl, ethyl, propyl,allyl, benzyl, butyl, pentyl, hexyl, or trimethylsilyl; m is an integerfrom 1 to 6, inclusive; and R^(4A) and R^(4B) are independently ahydrocarbyl group having up to 6 carbon atoms, or hydrogen.
 15. Theansa-metallocene of claim 11, wherein: M¹ is zirconium or hafnium; E isC or Si; X³ and X⁴ are independently H, BH₄, methyl, phenyl, benzyl,neopentyl, trimethylsilylmethyl, CH₂CMe₂Ph, CH₂SiMe₂Ph, CH₂CMe₂CH₂Ph, orCH₂SiMe₂CH₂Ph; R^(3A) and R^(3B) are independently a hydrocarbyl grouphaving up to 20 carbon atoms or a trihydrocarbylsilyl group having up to20 carbon atoms, or hydrogen; and R^(4A) and R^(4B) are independently ahydrocarbyl group having up to 12 carbon atoms, or hydrogen.
 16. Theansa-metallocene of claim 11, wherein: M¹ is zirconium or hafnium; E isC or Si; X³ and X⁴ are independently F, Cl, Br, or I; n is 1 or 2;R^(3A) and R^(3B) are independently H or methyl; m is 1 or 2; and R^(4A)and R^(4B) are independently H or t-butyl.
 17. A ligand for ametallocene polymerization catalyst, comprising: a compound having theformula:(X¹)(X²), wherein: X¹ and X² independently comprise a substitutedcyclopentadienyl, a substituted indenyl, or a substituted fluorenyl; X¹and X² are connected via a cyclic bridging moiety having the formulaE(Cyc), wherein E is a carbon atom, a silicon atom, a germanium atom, ora tin atom, and E is bonded to both X¹ and X², and wherein Cyc is asubstituted or an unsubstituted carbon chain of from 4 to 6 carbon atomsin length with each end of the carbon chain connected to E to form aring structure; and one substituent on X¹ or X² comprises a substitutedor an unsubstituted alkenyl group.
 18. The ligand of claim 17, whereinthe compound has the formula:

wherein: E is C or Si; n is an integer from 1 to 3, inclusive; R^(3A)and R^(3B) are independently a hydrocarbyl group, a trihydrocarbylsilylgroup, or hydrogen; m is an integer from 0 to 10, inclusive; and R^(4A)and R^(4B) are independently a hydrocarbyl group or hydrogen.
 19. Theligand of claim 17, wherein the compound has the formula:

wherein: R^(3A) and R^(3B) are independently H, methyl, ethyl, propyl,allyl, benzyl, butyl, pentyl, hexyl, or trimethylsilyl; m is an integerfrom 1 to 6, inclusive; and R^(4A) and R^(4B) are independently ahydrocarbyl group having up to 6 carbon atoms, or hydrogen.
 20. Theligand of claim 17, wherein the compound has the formula: